JP4830098B2 - Organic waste liquid combustion nozzle device and energy generation system - Google Patents

Organic waste liquid combustion nozzle device and energy generation system Download PDF

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JP4830098B2
JP4830098B2 JP2005199908A JP2005199908A JP4830098B2 JP 4830098 B2 JP4830098 B2 JP 4830098B2 JP 2005199908 A JP2005199908 A JP 2005199908A JP 2005199908 A JP2005199908 A JP 2005199908A JP 4830098 B2 JP4830098 B2 JP 4830098B2
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organic waste
waste liquid
combustion
air
nozzle
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JP2007017099A (en
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修一 鳥居
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国立大学法人 熊本大学
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23DBURNERS
    • F23D11/00Burners using a direct spraying action of liquid droplets or vaporised liquid into the combustion space
    • F23D11/36Details, e.g. burner cooling means, noise reduction means
    • F23D11/38Nozzles; Cleaning devices therefor
    • F23D11/386Nozzle cleaning
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G5/00Incineration of waste; Incinerator constructions; Details, accessories or control therefor
    • F23G5/44Details; Accessories
    • F23G5/442Waste feed arrangements
    • F23G5/446Waste feed arrangements for liquid waste
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G5/00Incineration of waste; Incinerator constructions; Details, accessories or control therefor
    • F23G5/44Details; Accessories
    • F23G5/46Recuperation of heat
    • 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
    • F23G7/008Incinerators or other apparatus for consuming industrial waste, e.g. chemicals for liquid waste
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2900/00Special features of, or arrangements for incinerators
    • F23G2900/54402Injecting fluid waste into incinerator
    • 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
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E20/00Combustion technologies with mitigation potential
    • Y02E20/12Heat utilisation in combustion or incineration of waste

Abstract

A combustion nozzle device for an organic waste liquid simply formed in a small structure, manufacturable at low cost, and installable in a small space by connecting with a heat source or a drive source apparatus, an energy generating system, and a burning treatment method for the organic waste liquid. An organic waste liquid force-feed tube (14), a supporting material force-feed tube (16), and an air force-feed tube (18) are communicably connected to the hollow part of a closed hollow container (12). The organic waste liquid, a supporting material, and air are simultaneously force-fed into the closed hollow container (12), and their mixed fluid is jetted from a jetting nozzle (20) for ignition and burning. The communication ports (34a) to (34d) of the air force-feed tube (18) are formed at positions more apart from the jetting nozzle (20) than a communication port (30) for the organic waste liquid force-feed tube (14) and a communication port (32) for the supporting material force-feed tube (16). Since the organic waste liquid can be easily fed by a force-feeding air and clogging is prevented from occurring, stable combustion can be sustained.

Description

本発明は有機質系廃液の燃焼ノズル装置、エネルギー発生システム及びその燃焼処理方法に係り、特に、食品製造分野、発酵工業あるいは畜産業などから排出される残渣液や尿などの有機系廃液を効果的に処理しかつ処理エネルギーを有効利用し得る装置等に関する。   The present invention relates to an organic waste liquid combustion nozzle device, an energy generation system, and a combustion treatment method thereof, and in particular, effectively uses organic waste liquid such as residual liquid and urine discharged from the food manufacturing field, fermentation industry or livestock industry. It is related with the apparatus etc. which can process and process energy effectively.

今日、大量生産・大量消費・大量廃棄型の社会経済活動が引き起こす都市・生活公害問題や地球規模の環境問題が深刻になってきており、特に、各種産業から排出される廃棄物の処理については公的な規制が適用されるのがほとんどである。廃棄物中の有機質系の廃液、例えば焼酎製造に伴う廃液、大豆等の煮汁廃液その他の種々の食品加工工程で廃棄される廃液、豚糞尿その他の畜産糞尿廃液等は、いずれも高いBOD(biochemical oxygen demand:生物化学的酸素要求量)、SS(suspended solid:水中懸濁有機無機物質)、COD(chemical oxygen demand:化学的酸素要求量)値を有し、そのままの状態で河川へ放流することは禁じられている。しかも、これらの廃液は種々の有機成分を含み、分離あるいは分解処理が困難で、しかも長期の放置により酸化が大きく進んで処理を困難にしている場合が多い。さらに、焼却処理場の建設や埋め立て処理地の確保はしだいに困難となっている。   Today, urban and lifestyle pollution problems and global environmental problems caused by mass production, mass consumption and mass disposal socio-economic activities are becoming more serious, especially for the treatment of waste discharged from various industries. Most public regulations apply. Organic waste liquids in waste, such as waste liquids from shochu production, boiled waste liquids such as soybeans, waste liquids discarded in various other food processing processes, pig manure and other livestock manure waste liquids, all have high BOD (biochemical It has oxygen demand (biochemical oxygen demand), SS (suspended solid: suspended organic matter in water), COD (chemical oxygen demand) values, and is discharged into the river as it is. Is forbidden. In addition, these waste liquids contain various organic components and are difficult to separate or decompose, and in many cases, oxidation is greatly advanced due to long-term standing, making the treatment difficult. Furthermore, it is becoming increasingly difficult to construct an incineration plant and secure a landfill site.

一例として、焼酎粕の処分では、その含水量が90〜95%含まれる高濃度廃液であるために固液分離が困難であり、有効な処理方法が模索されている。近年のエネルギー危機の中で、高含水有機性廃棄物から容易にエネルギーを回収できる手段としてメタン発酵が注目されており、この発酵は、高含水量、高濃度廃液を処理でき、ランニングコストが安い点で有利である。この方法では、含水率の高い有機系廃棄物の嫌気性発酵による処理が行なわれているものの、この処理には多大のエネルギー投入が必要で、実用化に難点がある。一方、レストラン等から排出される汚泥の焼却処理についての方法及び装置が特開平7-91636号において提案されている。
特開平7-91636号、0005、図1、図2
As an example, in the disposal of shochu, since it is a high-concentration waste liquid containing 90 to 95% of its water content, solid-liquid separation is difficult, and an effective treatment method is being sought. During the recent energy crisis, methane fermentation has attracted attention as a means of easily recovering energy from highly water-containing organic waste. This fermentation can treat high water content, high-concentration waste liquor, and low running costs. This is advantageous. In this method, the organic waste having a high water content is treated by anaerobic fermentation, but this treatment requires a large amount of energy input and has a difficulty in practical use. On the other hand, a method and apparatus for incineration of sludge discharged from a restaurant or the like is proposed in Japanese Patent Laid-Open No. 7-91636.
JP-A-7-91636, 0005, FIG. 1, FIG.

上記の特許文献1の方法ないし装置は、油水分離槽の上部に浮遊して溜まった油脂分を多く含む有機物からなる「スカム」の処理において、槽中の中間層の汚水の一部に界面活性剤等の添加剤を加えてこれを発泡容器に供給し、この発泡容器内で多数の気泡を形成させて該気泡を燃焼室に供給することにより、気泡中の水分を蒸発させるとともに、スカムや固形分残渣の可燃混合物を燃焼させ、灰燼化した固形分を回収するようにしたものである。しかしながら、特許文献1の装置では、燃焼に先立って気泡を発生しやすくするための攪拌破砕装置や界面活性剤、並びに気泡発生装置としての発泡容器が必要であり、システムが複雑化し高コストとなる。また、気泡容器での気泡発生のために水没させたチャンバに形成したパンチング孔の細孔を汚水に通過させる必要があるが、この際に目詰まりを生じやすく燃焼の前の気泡発生について装置運転時の管理が必要で、煩雑であった。また、汚水投入から燃焼までの間に複数の処理を必要とするから処理量が大きく制約され、そのぶん一次あるいは二次貯留槽を大型化させてコストや設置スペースについて不利であった。特に、ボイラやタービン等の機器の熱源としてシステム化する際には、汚水の燃焼工程のみに要する設備が長大化し、海浜沿い等の限られた地域でしか設置することが困難であった。さらに、その燃焼工程においては、燃焼中のガスバーナ11の火炎に気泡化された汚水と空気をあてて燃焼させるものであるから、十分な燃焼力を保持するために供給されるバーナの重油やガス等の燃焼用燃料コストが高くつくという問題があった。さらに、燃焼用の気泡送出スリット9g部分で、汚水が目詰まりしない確実性はなく、依然として装置稼働中のメンテナンス等を複数の装置あるいは部品について頻繁に行なう必要があった。   The method or apparatus of Patent Document 1 described above is based on the surface activity of a part of the sewage in the intermediate layer in the tank in the treatment of “scum” made of an organic substance containing a large amount of oil and fat suspended and collected in the upper part of the oil / water separation tank. An additive such as an agent is added and supplied to the foaming container. A large number of bubbles are formed in the foaming container, and the bubbles are supplied to the combustion chamber. The combustible mixture of the solid residue is burned to recover the ashed solid. However, the apparatus of Patent Document 1 requires a stirring and crushing apparatus and a surfactant for facilitating generation of bubbles prior to combustion, and a foaming container as the bubble generating apparatus, which complicates the system and increases costs. . In addition, it is necessary to pass through the punching holes formed in the submerged chamber for the generation of bubbles in the bubble container, and it is easy to cause clogging at this time. Time management was necessary and complicated. In addition, since a plurality of treatments are required between the input of sewage and combustion, the amount of treatment is greatly restricted, and the primary or secondary storage tank is enlarged, which is disadvantageous in terms of cost and installation space. In particular, when systemizing as a heat source for equipment such as boilers and turbines, the facilities required only for the combustion process of sewage have become long, and it has been difficult to install only in a limited area along the beach. Further, in the combustion process, since the bubbled sewage and air are applied to the flame of the burning gas burner 11 and burned, the burner heavy oil and gas supplied to maintain sufficient combustion power There is a problem that the cost of fuel for combustion is high. Further, there is no certainty that sewage is not clogged at the bubble sending slit 9g for combustion, and it is still necessary to frequently perform maintenance and the like for the plurality of devices or parts while the device is operating.

本発明は上記従来の課題に鑑みてなされたものであり、その1つの目的は簡単な構成で低コストであり、しかも小型の装置構成により小スペースでボイラやタービンその他の熱源あるいは駆動源機器と接続して設置し得る有機質系廃液の燃焼ノズル装置、エネルギー発生システム及びその燃焼処理方法を提供することにある。また、本発明の他の目的は、燃焼用燃費コストを大幅に低減できる有機質系廃液の燃焼ノズル装置、エネルギー発生システム及びその燃焼処理方法を提供することにある。さらに、本発明の他の目的は、簡単な構造により装置のメンテナンスや管理を簡単に行なえる有機質系廃液の燃焼ノズル装置、エネルギー発生システム及びその燃焼処理方法を提供することにある。   The present invention has been made in view of the above-described conventional problems, and one object of the present invention is a simple structure and low cost, and a small apparatus structure enables a boiler, a turbine, and other heat source or drive source equipment to be used in a small space. An object of the present invention is to provide an organic waste liquid combustion nozzle device, an energy generation system, and a combustion treatment method thereof that can be connected and installed. Another object of the present invention is to provide an organic waste liquid combustion nozzle device, an energy generation system, and a combustion treatment method thereof that can significantly reduce the fuel consumption cost for combustion. It is another object of the present invention to provide an organic waste liquid combustion nozzle device, an energy generation system, and a combustion treatment method thereof that can easily perform maintenance and management of the device with a simple structure.

上記の目的を達成するために、本発明は、中空閉鎖容器12と、中空閉鎖容器の中空部にそれぞれ異なる連通ポート30〜34で連通接続された有機質廃液圧送管14と、助燃材圧送管16と、空気圧送管18と、中空閉鎖容器内に圧送される有機質廃液と助燃材と空気との混合流体を大気側へ噴出させる噴出ノズル20と、を含み、有機質廃液と助燃材と空気とを同時に中空閉鎖容器12内に圧送し噴出ノズル20から噴出されるそれらの混合流体を燃材として着火燃焼させる有機質系廃液の燃焼ノズル装置であり、空気圧送管18の中空閉鎖容器12との連通ポート34a〜34dは、有機質廃液と助燃材とのそれぞれの中空閉鎖容器との連通ポート30、32よりも噴出ノズル20に対して、より離隔した位置に設定されており、さらに、中空閉鎖容器12の中空部は、空気圧送管18の連通ポート34a〜34dが連通する空気室38と、有機質廃液圧送管14と助燃材圧送16管の各連通ポート30,32が連通する混合室40と、を小通路36を中央にしてその両側に連通接続して設けられていることを特徴とする有機質系廃液の燃焼ノズル装置10から構成される。同一の中空閉鎖容器の中空部に対し、同時に複数の異なる連通ポートを介して有機質廃液と助燃材と空気とを圧送し、混合させて外部に噴出させる。比較的に大きな連通ポート孔から閉鎖容器内部に流体を導入させ、十分に混合した混合流体を比較的に小さな噴出ノズルから噴射させることで有機廃液や助燃材等の流動の際の目詰まりをしないようにさせつつ、燃焼に適した微粒子状ミストを確実に生成させてほとんどあらゆる有機廃液の燃焼、あるいは燃焼処理を実現する。また、単位時間当たりの処理量が多く、かつ、確実に処理できる。また、同一閉鎖容器内に圧送するだけであるから、特別の設備やコストは圧縮機以外には種火用バーナのみでよく、装置自体を小型で構成しうるうえに、製造コストも極めて低廉でよい。閉鎖容器の形状やサイズは任意に設定できるが、同時に廃液と助燃材と空気を注入するから、相互の圧送管内に他の圧送管からの流体を流入させないようにするとよい。さらに、目詰まりの原因を生じさせやすい大きな粒子の固形物を含む有機廃液や廃食油等を低圧側により近い位置に設定して混合作用と目詰まり防止機能を行なえる。空気が、下流側の場合で、空気の圧力が高い場合は、空気のみが噴出ノズルから噴出されやすくなる。この場合は少なくとも有機廃液と助燃材と略同じ圧送力で空気を中空部に圧送供給させる。 In order to achieve the above object, the present invention provides a hollow enclosure 12, an organic waste liquid pressure feed pipe 14 connected to the hollow portion of the hollow enclosure at different communication ports 30 to 34, and a combustion aid pressure feed pipe 16. A pneumatic feed pipe 18 and a jet nozzle 20 for jetting a mixed fluid of organic waste liquid, auxiliary combustion material and air pumped into the hollow closed container to the atmosphere side, the organic waste liquid, auxiliary combustion material and air At the same time, it is a combustion nozzle device for organic waste liquid that is ignited and combusted by using the mixed fluid ejected from the ejection nozzle 20 as a fuel material in the hollow enclosure 12, and the communication port of the pneumatic feed pipe 18 with the hollow enclosure 12. 34a~34d, to the jetting nozzle 20 than the communicating ports 30, 32 of the respective hollow enclosure with organic waste and improve combustion, is set to a more spaced position, further The hollow portion of the hollow enclosure 12 is mixed in the air chamber 38 through which the communication ports 34a to 34d of the pneumatic feeding pipe 18 communicate, and the communication ports 30 and 32 of the organic waste liquid pressure feeding pipe 14 and the auxiliary combustion material pressure feeding 16 pipe. The chamber 40 is provided with a combustion nozzle device 10 for organic waste liquid, characterized in that the chamber 40 is provided in communication with both sides of the small passage 36 at the center . The organic waste liquid, the auxiliary combustion material, and the air are simultaneously pumped through a plurality of different communication ports to the hollow portion of the same hollow closed container, mixed, and ejected to the outside. By introducing fluid into the closed container through a relatively large communication port hole and injecting a well-mixed fluid from a relatively small ejection nozzle, there is no clogging when the organic waste liquid or auxiliary material flows. In the meantime, almost all organic waste liquids are combusted or burned by reliably generating particulate mist suitable for combustion. In addition, the amount of processing per unit time is large and processing can be performed reliably. In addition, since it is only pumped into the same closed container, the special equipment and costs are only the seed burner other than the compressor, and the device itself can be made compact and the manufacturing cost is extremely low. Good. The shape and size of the closed container can be set arbitrarily, but since waste liquid, auxiliary combustion material, and air are injected at the same time, it is preferable not to allow fluid from other pumping pipes to flow into each other. Furthermore, the mixing action and the clogging prevention function can be performed by setting an organic waste liquid or waste cooking oil containing large solid particles that are likely to cause clogging at a position closer to the low pressure side. When the air is on the downstream side and the air pressure is high, only air is likely to be ejected from the ejection nozzle. In this case, at least air is pumped and supplied to the hollow portion with substantially the same pumping force as that of the organic waste liquid and the auxiliary combustion material.

その際に、小通路36は、噴出ノズル20のノズル孔20aの芯合わせ方向に長い通路からなるように構成するとより好ましい。   In that case, it is more preferable that the small passage 36 is constituted by a passage that is long in the alignment direction of the nozzle hole 20 a of the ejection nozzle 20.

また、小通路36を介して空気室38から混合室40へ空気を圧送する際の空気の流量を調節する調節弁機構44を設けるとよい。   Moreover, it is good to provide the adjustment valve mechanism 44 which adjusts the flow volume of the air at the time of pumping air from the air chamber 38 to the mixing chamber 40 via the small channel | path 36. FIG.

また、調節弁機構44は、ニードルの先端を小通路36の入り開口36aに突入するように進退移動するニードル弁装置50から構成するとよい。   Further, the adjustment valve mechanism 44 may be configured by a needle valve device 50 that moves forward and backward so that the tip of the needle enters the entrance opening 36 a of the small passage 36.

また、すくなくとも有機質廃液圧送管14と助燃材圧送管16とは、同じ圧縮装置66に連通されて有機質廃液と助燃材とが中空部に圧送されるようにするとなおよい。   Further, it is more preferable that at least the organic waste liquid pressure feeding pipe 14 and the auxiliary combustion material pressure feeding pipe 16 communicate with the same compression device 66 so that the organic waste liquid and the auxiliary combustion material are pressure fed to the hollow portion.

その際、少なくとも有機質廃液と助燃材とは略同じ圧送力で中空閉鎖容器12内に圧送されるようにするとよい。圧送力について多少の差圧が生じても燃焼反応は生じる。このとき、噴出ノズル(例えば噴出ノズルのノズル孔の径は数ミリメートルに設定する)は、大気に開放されているので、有機質廃液、助燃材(廃食油)、空気の混合流体は大気へ放出される。   At this time, at least the organic waste liquid and the auxiliary combustion material are preferably pumped into the hollow enclosure 12 with substantially the same pumping force. A combustion reaction occurs even if a slight pressure difference occurs in the pumping force. At this time, since the ejection nozzle (for example, the diameter of the nozzle hole of the ejection nozzle is set to several millimeters) is opened to the atmosphere, the mixed fluid of organic waste liquid, auxiliary combustion material (waste cooking oil), and air is released to the atmosphere. The

また、空気は有機質廃液又は助燃材と同じかあるいはそれらよりも高い圧力で圧送されるようにしてもよい。空気と、有機質廃液と助燃材とはそれぞれ同一圧力で中空閉鎖容器の中空部に圧送されると圧力バランスは安定し、ひいては燃焼自体を安定させる点でより好ましい。   Further, the air may be pumped at a pressure equal to or higher than that of the organic waste liquid or the auxiliary combustion material. When the air, the organic waste liquid, and the auxiliary combustion material are respectively pumped to the hollow portion of the hollow closed container at the same pressure, the pressure balance is stabilized, which is more preferable in terms of stabilizing the combustion itself.

また、中空閉鎖容器12に圧送される助燃材と有機質廃液とは容積比で1:1〜5:1で設定するとよい。   Moreover, it is good to set the auxiliary combustion material and organic waste liquid pumped by the hollow enclosure 12 by 1: 1 to 5: 1 by volume ratio.

また、本発明のエネルギー発生システムは、上記したいずれかの燃焼ノズル装置10の噴出ノズル20近傍に着火装置22を配置し、発生する燃焼エネルギーを熱源又は動力源として利用するように構成するとよい。   In addition, the energy generation system of the present invention may be configured such that the ignition device 22 is disposed in the vicinity of the ejection nozzle 20 of any one of the combustion nozzle devices 10 described above, and the generated combustion energy is used as a heat source or a power source.

また、中空閉鎖容器12に圧送する有機質廃液と助燃材との粘度に対応して噴出ノズル20の先端から着火装置22による着火位置までの距離を変更設定する着火位置可変機構74を有するようにするとよい。   In addition, an ignition position variable mechanism 74 that changes and sets the distance from the tip of the ejection nozzle 20 to the ignition position by the ignition device 22 corresponding to the viscosity of the organic waste liquid and the auxiliary combustion material to be pumped to the hollow closed container 12 is provided. Good.

本発明の有機質系廃液の燃焼ノズル装置は、中空閉鎖容器と、中空閉鎖容器の中空部にそれぞれ異なる連通ポートで連通接続された有機質廃液圧送管と、助燃材圧送管と、空気圧送管と、中空閉鎖容器内に圧送される有機質廃液と助燃材と空気との混合流体を大気側へ噴出させる噴出ノズルと、を含み、有機質廃液と助燃材と空気とを同時に中空閉鎖容器内に圧送し噴出ノズルから噴出されるそれらの混合流体を燃材として着火燃焼させる構成であるから、簡単な構成で低コストであり、しかも小型の装置構成により小スペースでボイラやタービンその他の熱源あるいは駆動源機器へ駆動エネルギーを供給させることができる。また、基本的にどのような特性の有機廃液でも燃焼させることができるから、河川放流に頼らざるを得なかった焼酎廃液、大豆煮汁や、地中吸い込み、貯留、埋め立て処理等しか対策がなかった動物糞尿処理等について、効果的に処理ができ、しかもエネルギー源として有効活用しうる。さらに、燃焼用燃費コストを大幅に低減でき、しかも、簡単な構造により故障が少なく、しかも、装置のメンテナンスや管理を簡易に行なえる。   An organic waste liquid combustion nozzle device according to the present invention includes a hollow closed container, an organic waste liquid pressure feed pipe connected to the hollow portion of the hollow closed container through different communication ports, an auxiliary combustion material pressure feed pipe, a pneumatic feed pipe, An ejection nozzle that ejects a mixed fluid of organic waste liquid, auxiliary combustion material, and air pumped into the hollow enclosure to the atmosphere, and simultaneously discharges the organic waste liquid, auxiliary combustion material, and air into the hollow enclosure Since the mixed fluid ejected from the nozzle is ignited and burned as a fuel, it is simple and low-cost, and it can be used in boilers, turbines, and other heat source or drive source equipment in a small space thanks to its compact configuration. Driving energy can be supplied. In addition, organic waste liquid of any characteristics can be combusted basically, so there were only measures such as shochu waste liquid, soybean soup that had to be relied on river discharge, underground suction, storage, landfill treatment, etc. Animal feces and urine can be treated effectively, and can be effectively used as an energy source. In addition, the fuel cost for combustion can be greatly reduced, and the simple structure has few failures, and the maintenance and management of the apparatus can be performed easily.

また、少なくとも有機質廃液と助燃材とは略同じ圧送力で中空閉鎖容器内に圧送される構成とすることにより、相互の圧送管への逆流を防ぎ、両者の投入量バランスを安定させて混合流体の構成比を一定化させ、安定した燃焼を保持させることができる。   In addition, at least the organic waste liquid and the auxiliary combustion material are configured to be pumped into the hollow closed container with substantially the same pumping force, so that backflow to the pumping tube is prevented, and the balance of the input amount of both is stabilized and the mixed fluid The composition ratio can be made constant, and stable combustion can be maintained.

また、空気は有機質廃液又は助燃材と略同じかあるいはそれらよりも高い圧力で圧送されるようにすることにより、有機質廃液又は助燃材の空気圧送管側への逆流を防止すると同時に、十分な酸素量の供給と噴出ノズル側への圧送を確実に行なうことが可能である。   In addition, air is pumped at a pressure substantially the same as or higher than that of organic waste liquid or auxiliary combustion material, thereby preventing backflow of the organic waste liquid or auxiliary combustion material to the pneumatic feeding pipe side and sufficient oxygen. It is possible to reliably perform the supply of the amount and the pressure feeding to the ejection nozzle side.

また、空気圧送管の中空閉鎖容器との連通ポートは、有機質廃液と助燃材とのそれぞれの中空閉鎖容器との連通ポートよりも噴出ノズルに対して、より離隔した位置に設定された構成とすることにより、有機質廃液と助燃材がより噴出ノズルに近接した位置、すなわち、低圧側の外気に近い位置にそれらの有機質廃液や助燃材が注入される結果、圧送空気が有機廃液を送風しやすい状態となる。そして、目詰まり等を生じにくくさせることができ、安定した燃焼を持続させることができる。   Further, the communication port of the pneumatic feeding tube with the hollow closed container is configured to be set at a position further away from the ejection nozzle than the communication port of the organic waste liquid and the auxiliary combustion material with each hollow closed container. As a result, the organic waste liquid and the auxiliary combustion material are injected closer to the position near the ejection nozzle, that is, the position near the low-pressure side outside air, and as a result, the compressed air easily blows the organic waste liquid. It becomes. And it can make it hard to produce clogging etc. and can maintain the stable combustion.

また、中空閉鎖容器の中空部は、空気圧送管の連通ポートが連通する空気室と、有機質廃液圧送管と、助燃材圧送管の各連通ポートが連通する混合室と、を小通路を中央にしてその両側に連通接続して設けられた構成であるから、有機質廃液と助燃材をより噴出ノズルに近接した低圧側に近い位置に注入させて、目詰まり等を生じにくくさせる上に、コンプレッサ等の空気圧供給源から受けた空気をビーム状に混合室側に圧送でき、噴出ノズル側への圧送力を確保しうる。また、ノズルの直前に混合室があるので、この部分で圧力変動をある程度緩和でき、燃焼を安定させることができる。   In addition, the hollow portion of the hollow closed container has a small passage in the center with an air chamber that communicates with the communication port of the pneumatic feeding tube, an organic waste liquid pressure feeding tube, and a mixing chamber that communicates with each communication port of the auxiliary combustion material pressure feeding tube. In order to prevent clogging and the like by injecting the organic waste liquid and the auxiliary combustion material closer to the low pressure side closer to the ejection nozzle, it is possible to prevent clogging. The air received from the air pressure supply source can be pumped to the mixing chamber side in the form of a beam, and the pumping force to the jet nozzle side can be secured. Further, since there is a mixing chamber immediately before the nozzle, the pressure fluctuation can be alleviated to some extent in this portion, and combustion can be stabilized.

また、小通路は、噴出ノズルのノズル孔の芯合わせ方向に長い通路からなる構成であるから、小通路からのビーム状の空気は混合室で他の要素と混合して混合流体とし、流れのエネルギーを大幅に損なわずにそのままノズル孔から外部に噴出されてエネルギーロスを少なくしつつ良質の微粒子状ミストを発生させることができる。   Further, since the small passage is composed of a passage that is long in the alignment direction of the nozzle hole of the ejection nozzle, the beam-like air from the small passage is mixed with other elements in the mixing chamber to form a mixed fluid, It is possible to generate fine particulate mist while reducing energy loss by being ejected from the nozzle hole as it is without significantly losing energy.

また、小通路を介して空気室から混合室へ空気を圧送する際の空気の流量を調節する調節弁機構が設けられた構成とすることにより、混合室で生成される混合流体中の空気量の調整を処理対象の有機質廃液や、あるいは助燃材の特性に対応して自在に調節設定することが可能である。   In addition, the amount of air in the mixed fluid generated in the mixing chamber is provided by a control valve mechanism that adjusts the flow rate of air when the air is pumped from the air chamber to the mixing chamber via the small passage. It is possible to freely adjust the setting according to the characteristics of the organic waste liquid to be treated or the auxiliary combustion material.

また、調節弁機構は、ニードルの先端を小通路の入り開口に突入するように進退移動するニードル弁装置からなる構成であるから、例えば操作部分を外部に突設させておくことにより、ニードルの進退移動のみで高精度でかつ微調整の空気流量調整設定を行える。   Further, since the control valve mechanism is composed of a needle valve device that moves forward and backward so that the tip of the needle projects into the entrance opening of the small passage, for example, by projecting the operation portion to the outside, High precision and fine adjustment of the air flow rate can be set only by moving forward and backward.

また、すくなくとも有機質廃液圧送管と助燃材圧送管とは、同じ圧縮装置に連通されて有機質廃液と助燃材とが中空部に圧送される構成とすることにより、中空部から相互の圧送管側に媒体が逆流して注入量バランスを損なうことなく、安定した、確実な燃焼処理を実現し得る。   In addition, at least the organic waste liquid pressure feeding pipe and the auxiliary combustion material pressure feeding pipe are connected to the same compression device so that the organic waste liquid and the auxiliary combustion material are pumped to the hollow part, so that the hollow part moves from the hollow part to the mutual pressure feeding pipe side. A stable and reliable combustion process can be realized without the medium flowing backward and impairing the injection amount balance.

また、中空閉鎖容器に圧送される助燃材と有機質廃液とが容積比で1:1〜5:1で設定されている構成とすることにより、噴出ノズルから噴出される微粒子状ミストの燃焼を維持することができる。   Moreover, the combustion of the particulate mist ejected from the ejection nozzle is maintained by adopting a configuration in which the auxiliary combustion material and the organic waste liquid pumped to the hollow closed container are set at a volume ratio of 1: 1 to 5: 1. can do.

また、本発明の有機質系廃液のエネルギー発生システムは、請求項1ないし10のいずれかの燃焼ノズル装置の噴出ノズル近傍に着火装置を配置し、発生する燃焼エネルギーを熱源又は動力源として利用する構成であるから、廃棄物を簡易な構成で燃焼して廃棄物処理を簡易に行なえるうえに、その際に発生する燃焼エネルギーを利用して熱源あるいは動力源に対してエネルギー供給を行なえ、有価物として機能し得る。   An organic waste liquid energy generation system according to the present invention has a configuration in which an ignition device is disposed in the vicinity of an ejection nozzle of a combustion nozzle device according to any one of claims 1 to 10 and the generated combustion energy is used as a heat source or a power source. Therefore, waste can be burned with a simple configuration and waste disposal can be easily performed. In addition, the combustion energy generated at that time can be used to supply energy to a heat source or power source. Can function as.

また、中空閉鎖容器に圧送する有機質廃液と助燃材との粘度に対応して噴出ノズルの先端から着火装置による着火位置までの距離を変更設定する着火位置可変機構を有する構成であるから、有機質廃液や助燃材の粘度に対応した最良の燃焼点で着火させて効率のよい火炎生成を行なって燃焼効率を向上させることができる。   In addition, the organic waste liquid is configured to have an ignition position variable mechanism that changes and sets the distance from the tip of the ejection nozzle to the ignition position by the ignition device in accordance with the viscosity of the organic waste liquid and the auxiliary combustion material to be pumped to the hollow closed container. In addition, it is possible to improve the combustion efficiency by generating an efficient flame by igniting at the best combustion point corresponding to the viscosity of the auxiliary combustion material.

また、有機質系廃液の燃焼処理方法によれば、それぞれ別個のポートで中空閉鎖容器に連通する供給管を介して有機質廃液と、助燃材と、空気と、を同時に略同圧で圧送し、中空閉鎖容器に設けた噴出ノズルから有機質廃液と助燃材と空気との混合流体を噴出させ、該噴出流体に着火させることにより燃焼させる構成であるから、簡単な構成で、しかも小型の装置構成により小スペースで熱源あるいは駆動源機器へ駆動エネルギーを供給させることができる。また、基本的にどのような特性の有機廃液でも燃焼させることができるから、河川放流に頼らざるを得なかった焼酎廃液、大豆煮汁や、地中吸い込み、貯留、埋め立て処理等しか対策がなかった動物糞尿処理等について、効果的に処理ができ、しかもエネルギー源として有効活用しうる。さらに、燃焼用燃費コストを大幅に低減できる。   Further, according to the organic waste liquid combustion treatment method, the organic waste liquid, the auxiliary combustion material, and the air are simultaneously pumped at substantially the same pressure through a supply pipe that communicates with the hollow closed container through separate ports, Since the mixed fluid of organic waste liquid, auxiliary combustion material, and air is ejected from the ejection nozzle provided in the closed container and burned by igniting the ejected fluid, it is simple and small in size with a small device configuration. Drive energy can be supplied to a heat source or a drive source device in a space. In addition, organic waste liquid of any characteristics can be combusted basically, so there were only measures such as shochu waste liquid, soybean soup that had to be relied on river discharge, underground suction, storage, landfill treatment, etc. Animal feces and urine can be treated effectively, and can be effectively used as an energy source. Furthermore, the fuel cost for combustion can be greatly reduced.

以下、添付図面を参照しつつ本発明を実施するための最良の形態について説明する。図1ないし図4は、本発明の有機質系廃液の燃焼ノズル装置の第1実施形態を示している。本発明の有機質系廃液の燃焼ノズル装置は、食品製造分野、発酵工業分野あるいは畜産業などから排出される残渣液や尿などを効果的に燃焼し、さらにその燃焼エネルギーを簡易に有効利用し得る装置であり、特に、装置構成が極めて簡単で、小型であり、製造ならびにメンテナンスコストを低廉に保持させ、さらに、燃焼用の燃料を大幅に節約することのできる装置である。本発明の有機質系廃液の燃焼ノズル装置が処理対象とする有機質系廃液は、焼酎廃液(焼酎滓)、大豆等の煮汁廃液その他の種々の食品加工工程で廃棄される廃液、豚、鶏、牛等の糞尿その他の畜産糞尿廃液その他の有機質系廃液であり、予め例えばフィルタプレスや遠心分離機等で有機固形物、無機固形物を除去した後の廃液(前処理後の廃液)であり、最終的に大気側に噴出させる噴出ノズルの少なくとも開口径以上の大きさの固形物を除いた後の廃液の処理を行なう。   The best mode for carrying out the present invention will be described below with reference to the accompanying drawings. 1 to 4 show a first embodiment of an organic waste liquid combustion nozzle device of the present invention. The organic waste liquid combustion nozzle device of the present invention can effectively burn residual liquid and urine discharged from the food production field, fermentation industry field, livestock industry, etc., and can easily and effectively use the combustion energy. In particular, the apparatus has a very simple apparatus configuration, is small in size, can maintain manufacturing and maintenance costs at a low cost, and can greatly save fuel for combustion. The organic waste liquid to be processed by the organic waste liquid combustion nozzle device of the present invention includes shochu waste liquid (shochu), boiled waste liquid such as soybeans, and other waste liquids discarded in various food processing processes, pigs, chickens, cattle Such as manure and other livestock manure waste liquids and other organic waste liquids such as waste liquids after removing organic solids and inorganic solids with a filter press or a centrifuge in advance (waste liquid after pretreatment) The waste liquid is processed after removing the solid matter having a size larger than at least the opening diameter of the ejection nozzle that is ejected to the atmosphere side.

図1は、本発明の有機質系廃液の燃焼ノズル装置10を含む燃焼装置110の概略構成説明図であり、図において、本発明の有機質系廃液の燃焼ノズル装置10は、中空閉鎖容器12と、中空閉鎖容器の中空部にそれぞれ別の通路で連通接続された有機質廃液圧送管14と、助燃材圧送管16と、空気圧送管18と、中空閉鎖容器の一端側に設けられた噴出ノズル20と、を含む。そして、噴出ノズル20から有機質廃液と、助燃材と、空気との混合流体が外部あるいは大気側、例えば燃焼室150側に噴出されて着火手段22により着火されて燃焼する。   FIG. 1 is an explanatory diagram of a schematic configuration of a combustion apparatus 110 including an organic waste liquid combustion nozzle apparatus 10 according to the present invention. In the figure, an organic waste liquid combustion nozzle apparatus 10 according to the present invention includes a hollow enclosure 12, An organic waste liquid pressure feed pipe 14, an auxiliary combustor pressure feed pipe 16, a pneumatic pressure feed pipe 18, and a jet nozzle 20 provided on one end of the hollow closed container, each connected to a hollow portion of the hollow closed container by a separate passage. ,including. Then, a mixed fluid of the organic waste liquid, the auxiliary combustion material, and the air is ejected from the ejection nozzle 20 to the outside or the atmosphere side, for example, the combustion chamber 150 side, and is ignited and combusted by the ignition means 22.

図において、中空閉鎖容器12は、有機質系廃液の燃焼ノズル装置10の主要な部分を構成する構造体であり、その中空内部に同時に略同圧圧送される空気と処理すべき有機質廃液と助燃材とを受け入れて混合流体として噴出ノズル20から微粒子のミスト状態で噴出させる燃焼用流体発生手段である。実施形態において、中空閉鎖容器12は、耐熱素材からなる閉鎖ケースからなり、例えばステンレス製で形成されて全体としては中空の円筒形状で構成されている。実施形態では、この中空閉鎖容器のサイズは例えば直径3cm、長さ10cm程度の小型の円筒状ケース体から構成されているが、それ以上か、それ以下のサイズでもよい。   In the figure, a hollow enclosure 12 is a structure that constitutes a main part of an organic waste liquid combustion nozzle device 10, air that is simultaneously pumped into the hollow at the same pressure, an organic waste liquid to be treated, and a combustion aid. Is a combustion fluid generating means for receiving the gas as a mixed fluid and ejecting it from the ejection nozzle 20 in a mist state of fine particles. In the embodiment, the hollow closed container 12 is formed of a closed case made of a heat-resistant material, and is formed of, for example, stainless steel and has a hollow cylindrical shape as a whole. In the embodiment, the size of the hollow enclosure is composed of, for example, a small cylindrical case body having a diameter of about 3 cm and a length of about 10 cm, but it may be larger or smaller.

実施形態において、中空閉鎖容器12は、円筒の両端壁121と、周壁122と、を有する円筒形状で構成され、複数の構成要素を一体的に組み付け接合させて構成されている。図1、図3において、円筒形状の一端(121a)側に混合流体を噴出させる噴出ノズル20を形成し、そのノズル孔を介して中空内部と外部とを連通させている。噴出ノズル20は微粒子状ミスト発生構造を有しており、実施形態では、中空内部との連通路をいったん絞ってオリフィス状出口20aを形成し、このオリフィス状出口から外部方向に向けて出口をしだいに拡大するようにテーパ流路26を設けて構成している。すなわち、微粒子状ミスト発生構造は、オリフィス状出口20aを有するオリフィス部24と、これに連続して拡大するテーパ流路26と、を有している。オリフィス状出口20aは、有機質系廃液と助燃材と空気との混合流体の外部への出口で最も狭い流路部分であり、実施形態では、このオリフィス状出口20aがノズル孔とされる。本実施形態において、オリフィス状出口20aは、例えば直径1〜2mm程度に設定されており、5mm直径程度の各連通ポートから圧送される流体が目詰まりなく安定して確実に閉鎖容器内部に注入する一方、中空部で混合した混合流体をノズル孔からの低圧開放により確実に微粒子状ミスト化して燃焼を促進させることができる。実施形態では最狭小通路としてのオリフィス状出口20aよりも内側となる端壁121aの部分には漏斗状にしだいに進行方向(中空閉鎖容器の内側から外側に向けて)に向けて通路を小さくする拡小テーパ流路28が設けられてその拡小テーパ流路28の先端部がオリフィス状出口20aに連続して設けられている。拡大テーパ流路26は、高圧高速の混合流体がオリフィス状出口20aの出口開口(20a)から放出される際に発生する微粒子状のミストをその流路を拡大させつつ拡散させるように外部に向けて放出案内する手段である。実施形態において、オリフィス状出口20aの流路中心線r1は中空閉鎖容器の円筒軸線c1に一致するように形成されており、したがって、混合流体は該円筒軸線上あるいはこれに沿って噴出ノズル20から噴出される。   In the embodiment, the hollow closed container 12 is formed in a cylindrical shape having both cylindrical end walls 121 and a peripheral wall 122, and is configured by integrally assembling and joining a plurality of components. 1 and 3, an ejection nozzle 20 for ejecting a mixed fluid is formed on the cylindrical end (121a) side, and the hollow interior and the exterior are communicated with each other through the nozzle hole. The ejection nozzle 20 has a fine particle mist generating structure. In the embodiment, the orifice-like outlet 20a is formed by once narrowing the communication path with the hollow interior, and the outlet gradually increases from the orifice-like outlet toward the outside. The taper flow path 26 is provided so as to be enlarged. That is, the fine particle mist generating structure has an orifice portion 24 having an orifice-like outlet 20a and a taper channel 26 that continuously expands. The orifice-shaped outlet 20a is the narrowest flow path portion to the outside of the mixed fluid of the organic waste liquid, the auxiliary combustion material, and the air. In the embodiment, the orifice-shaped outlet 20a is a nozzle hole. In the present embodiment, the orifice-shaped outlet 20a is set to have a diameter of about 1 to 2 mm, for example, and fluid pumped from each communication port having a diameter of about 5 mm is stably and surely injected into the closed container without clogging. On the other hand, the mixed fluid mixed in the hollow portion can be surely made into a fine mist by releasing the low pressure from the nozzle hole to promote combustion. In the embodiment, the portion of the end wall 121a on the inner side of the orifice-shaped outlet 20a as the narrowest narrow passage gradually decreases in the direction of travel (from the inner side to the outer side of the hollow enclosure) in the funnel shape. An enlarged taper channel 28 is provided, and the tip of the enlarged taper channel 28 is provided continuously with the orifice outlet 20a. The enlarged taper channel 26 is directed outward so as to diffuse the fine particle mist generated when the high-pressure and high-speed mixed fluid is discharged from the outlet opening (20a) of the orifice-shaped outlet 20a while expanding the channel. It is a means to guide the release. In the embodiment, the flow path center line r1 of the orifice-shaped outlet 20a is formed so as to coincide with the cylindrical axis c1 of the hollow enclosure, so that the mixed fluid is discharged from the ejection nozzle 20 on or along the cylindrical axis. Erupted.

中空閉鎖容器12の周壁122には各圧送管の連通接続用の複数のポートが設けられている。実施形態において、図2、3、4に示すように、噴出ノズル20寄り側の周壁122において、直径方向に対向する位置に2個の第1、第2連通ポート30,32が、並びにそれらから噴出ノズル20に対してより離隔する位置に4個の第3、第4、第5、第6連通ポート34a、34b、34d、34eの計6個の連通ポートが円筒容器の半径方向に貫通するように設けられている。各連通ポート30〜34は、中空閉鎖容器12の中空部にそれぞれ異なる位置に設けられて連通する連通手段であり、周壁122の壁を貫通する方向にそれぞれ孔30p〜34epを形成して中空内部と各圧送管とをそれぞれ別の流路で連通させる。本実施形態では各連通ポートは、閉鎖容器本体の連通孔に一端側を連通接続し、他端側の一部を容器の半径方向に突設させたポート用金具で構成されている。第1連通ポート30には有機質系廃液圧送管14が連結接続され、第2連通ポート32には助燃材圧送管16が連結接続され、さらに第3から第6の連通ポートにはそれぞれ空気圧送管18が連結接続されている。これらの連通ポートの孔は本実施形態では例えば5mm程度に設定されている。例えば、実施形態程度の全体サイズで有機質系廃液が流入する混合室容積が1.2cmで設定されており、例えばこの場合には、連通ポートの孔(空気室あるいは混合室との連通孔)の径Dpは5mm〜7mm程度に設定するとよい。 The peripheral wall 122 of the hollow enclosure 12 is provided with a plurality of ports for communication connection of each pressure feeding tube. In the embodiment, as shown in FIGS. 2, 3, and 4, in the peripheral wall 122 closer to the ejection nozzle 20, the two first and second communication ports 30 and 32 are arranged at positions opposed to each other in the diametrical direction. A total of six communication ports of four third, fourth, fifth, and sixth communication ports 34a, 34b, 34d, and 34e penetrate in the radial direction of the cylindrical container at positions farther from the ejection nozzle 20. It is provided as follows. The communication ports 30 to 34 are communication means that are provided at different positions in the hollow portion of the hollow enclosure 12 and communicate with each other, and form holes 30p to 34ep in the direction penetrating the wall of the peripheral wall 122, respectively. And the pressure feeding pipes communicate with each other through different flow paths. In the present embodiment, each communication port is constituted by a port metal fitting in which one end side is connected to the communication hole of the closed container body and a part on the other end side protrudes in the radial direction of the container. An organic waste liquid pressure feed pipe 14 is connected to the first communication port 30, an auxiliary combustion material pressure feed pipe 16 is connected to the second communication port 32, and a pneumatic feed pipe is connected to each of the third to sixth communication ports. 18 are connected and connected. In this embodiment, the holes of these communication ports are set to about 5 mm, for example. For example, the volume of the mixing chamber into which the organic waste liquid flows in with the overall size of the embodiment is set to 1.2 cm 2. For example, in this case, the hole of the communication port (the communication hole with the air chamber or the mixing chamber) The diameter Dp may be set to about 5 mm to 7 mm.

さらに、図3にも示すように、中空閉鎖容器12の中空内部は、中間に小通路36を介してこの小通路36に連通するように空気室38と混合室40とを配して構成されている。小通路36は空気室38側に圧送供給された空気を混合室40側に供給する空気の通路であり、実施形態において、円筒状の中空閉鎖容器の中間位置において円筒の軸線上にその中心軸線を位置させた細長い空気の通路からなる。そして、この小通路36と両端の空気室38及び混合室40は、円筒状の閉鎖容器12の内部にダンベル状の中空部を一体的に形成するように、該閉鎖容器12は組み付け接合されている。すなわち、空気室38及び混合室40は小通路36の両端に連通接続されて、該通路36から段付き状にそれぞれ拡大した短円筒形状の中空部からなり、空気室38、小通路36、混合室40は直線列状に配置されていてそれらの中心線は噴出ノズル20のノズル孔(オリフィス状出口)と芯合わせ位置となるように形成されている。噴出ノズル20に近い室が有機廃液と助燃材とが同時に略同圧で圧送される混合室40であり、混合室40は噴出ノズル20の拡小テーパ流路28の内側空隙と(拡小テーパ流路の最大径部分)連通しており、これによって、混合室40内とノズル孔20a並びに容器12外部とを連通させている。42は、中空閉鎖容器の本体に噴出ノズル20部分を組み付けた際の気密のためのパッキンである。混合室40には、第1及び第2の連通ポート30,32が円筒容器の直径方向の両端位置に連通接続されて有機廃液並びに助燃材を圧送する。前記したように、これらのポートの孔は略同じ直径で構成され略同圧で圧送されて流入する。これは混合室40内で充填圧力の差があれば高いほうの圧力で流入する廃液あるいは助燃材が低圧で圧入されるもののほうのポートの孔から各圧送管内に流入し一部の流体を逆流させて、混合室内でのそれらの混合バランスを崩すおそれがあるからである。その意味では、厳密には、有機廃液及び助燃材の圧送力は混合室内での他のポート孔への圧入が生じない程度の圧力で、という意味であって、同圧あるいは同圧でなくともよいが、いずれにしても大気圧以上の圧力により、混合室内でのそれらの混合バランスを崩さない程度の圧力差を許容限度として任意に設定できる。空気室38は空気が圧送されて流入する室であり、混合室の直径と例えば略同一径であって一端を閉鎖容器の円筒の他端側に延長し開放した空間で形成されている。なお、この閉鎖容器の本体の他端側開放部は当然のことながら外部に対しては閉鎖されており、本実施形態では、後述する調節弁機構を介して気密閉鎖されている。図2に示すように周方向に90度ずつずらした位置に設定した第3〜第6ポート34a〜34dから空気室38内に圧力空気が導入される。本実施形態では空気室38に圧送された空気は小通路36を通って混合室40を経由し、さらに低圧開放端側のオリフィス状出口20aに向けて直線状に流れる。一方、混合室内の有機廃液と助燃材とは円筒容器の半径方向に貫通するように混合室40に流入しそれぞれが高速流体で一気に混合されて混合流体としてオリフィス状出口20aから噴出される。 Further, as shown in FIG. 3, the hollow interior of the hollow enclosure 12 is configured by arranging an air chamber 38 and a mixing chamber 40 so as to communicate with the small passage 36 through a small passage 36 in the middle. ing. The small passage 36 is an air passage for supplying air fed to the air chamber 38 side to the mixing chamber 40 side. In the embodiment, the small passage 36 has a central axis on the axis of the cylinder at an intermediate position of the cylindrical hollow enclosure. It consists of a long and narrow air passage. The small container 36 and the air chamber 38 and the mixing chamber 40 at both ends are assembled and joined so that a dumbbell-shaped hollow portion is integrally formed in the cylindrical closed container 12. Yes. That is, the air chamber 38 and the mixing chamber 40 is communicatively connected to both ends of the small passage 36, a hollow portion of the short cylindrical enlarged from each of the small passage 36 in stepped, air chamber 38, a small passage 36, The mixing chambers 40 are arranged in a straight line, and their center lines are formed so as to be aligned with the nozzle holes (orifice-shaped outlets) of the ejection nozzle 20. A chamber close to the ejection nozzle 20 is a mixing chamber 40 in which the organic waste liquid and the auxiliary combustion material are simultaneously pumped at substantially the same pressure, and the mixing chamber 40 is an inner space of the expansion taper channel 28 of the ejection nozzle 20 (an expansion taper). The maximum diameter portion of the flow path) communicates with each other, thereby communicating the inside of the mixing chamber 40 with the nozzle hole 20a and the outside of the container 12. 42 is an airtight packing when the jet nozzle 20 portion is assembled to the main body of the hollow closed container. In the mixing chamber 40, first and second communication ports 30 and 32 are connected to both ends of the cylindrical container in the diametrical direction to pressure-feed the organic waste liquid and the auxiliary combustion material. As described above, the holes of these ports are formed with substantially the same diameter, and are pumped at approximately the same pressure and flow in. This is because if there is a difference in filling pressure in the mixing chamber 40, waste liquid or auxiliary combustible material that flows in at a higher pressure flows into each pumping pipe from the port hole of the one that is injected at a lower pressure, and some fluid flows backward. This is because the mixing balance in the mixing chamber may be lost. In that sense, strictly speaking, the pumping force of the organic waste liquid and the auxiliary combustor is a pressure that does not cause press-fitting into other port holes in the mixing chamber, and it does not require the same pressure or the same pressure. In any case, a pressure difference that does not disturb the mixing balance in the mixing chamber due to a pressure higher than atmospheric pressure can be arbitrarily set as an allowable limit. The air chamber 38 is a chamber into which air is pumped and flows, and is formed in a space that is, for example, substantially the same diameter as the mixing chamber and has one end extended to the other end of the cylinder of the closed container and opened. Note that the open portion on the other end side of the main body of the closed container is naturally closed to the outside, and in the present embodiment, it is hermetically sealed via a regulating valve mechanism described later. As shown in FIG. 2, pressurized air is introduced into the air chamber 38 from the third to sixth ports 34 a to 34 d set at positions shifted by 90 degrees in the circumferential direction. In the present embodiment, the air pressure-fed to the air chamber 38 flows in a straight line through the small passage 36, the mixing chamber 40, and further toward the orifice-shaped outlet 20a on the low-pressure open end side. On the other hand, the organic waste liquid and the auxiliary combustion material in the mixing chamber flow into the mixing chamber 40 so as to penetrate in the radial direction of the cylindrical container, are mixed at once with a high-speed fluid, and are ejected from the orifice-shaped outlet 20a as a mixed fluid.

図1、3において、円筒状の閉鎖容器の他端側には調節弁機構44が設けられ、この調節弁機構44の要素を介して円筒の他端側は閉鎖されている。調節弁機構44は、小通路36を介して空気室38から混合室40へ空気を圧送する際の空気の流量を調節する空気流量調節手段であり、本実施形態では中空閉鎖容器の直径よりも小さな直径の軸体ホルダ46とホルダの先端に取り付けたニードル弁48と、を含むニードル弁装置50を有している。軸体ホルダ46は閉鎖容器12の円筒軸と軸の方向を同じとするように中空閉鎖容器の空気室38の延長部39の内壁に形成されためねじ孔52に螺合され、小通路36の流路軸方向に螺進退自在に移動するボルト軸体から構成されている。この軸体ホルダ46は、閉鎖容器本体開放端側の内壁に取り付けられたパッキン54を密着摺動自在に貫通して閉鎖容器12の内外を気密閉鎖する。軸体ホルダ46の円筒軸体の一部は外部に突出して設けられ、その突出端には操作突周56が形成されている。軸体ホルダ46の外部突出部分が操作摘み部58を形成する。軸体ホルダ46はその外部突出側の反対側の端部にニードル弁48を固定している。ニードル弁48は、その先端が小通路36の入り開口36aに突入するように進退移動し、空気圧送用の第3の連通ポート34a〜34dから圧送される空気の空気室38から小通路36への流入量を調節する。この場合、ニードル弁48の先端はニードルの軸心に向けて尖っており、したがって、小通路36の入り開口36aに近接する際にニードルの先端尖り部表面と入り開口36aとの隙間が尖り部の周囲に均等に形成されるから安定した流れで空気が小通路36内に入り、混合室40側に流入する。   1 and 3, a control valve mechanism 44 is provided on the other end side of the cylindrical closed container, and the other end side of the cylinder is closed via an element of the control valve mechanism 44. The adjustment valve mechanism 44 is an air flow rate adjusting means for adjusting the flow rate of air when the air is pumped from the air chamber 38 to the mixing chamber 40 via the small passage 36. In this embodiment, the control valve mechanism 44 is more than the diameter of the hollow enclosure. It has a needle valve device 50 including a small diameter shaft holder 46 and a needle valve 48 attached to the tip of the holder. The shaft body holder 46 is formed on the inner wall of the extension 39 of the air chamber 38 of the hollow enclosure so as to have the same axial direction as the cylindrical axis of the enclosure 12, and is screwed into the screw hole 52. It is comprised from the volt | bolt shaft body which moves to the flow-path axis direction so that screwing back and forth is possible. This shaft body holder 46 tightly and slidably penetrates the packing 54 attached to the inner wall on the open end side of the closed container main body so as to hermetically seal the inside and outside of the closed container 12. A part of the cylindrical shaft body of the shaft body holder 46 protrudes to the outside, and an operation protrusion 56 is formed at the protruding end. An external projecting portion of the shaft body holder 46 forms an operation knob 58. The shaft body holder 46 has a needle valve 48 fixed to the end opposite to the external projecting side. The needle valve 48 advances and retreats so that the tip of the needle valve 48 enters the entrance opening 36 a of the small passage 36, and is supplied from the air chamber 38 for air pressure fed from the third communication ports 34 a to 34 d for supplying pneumatic pressure to the small passage 36. Adjust the amount of inflow. In this case, the tip of the needle valve 48 is pointed toward the axial center of the needle. Therefore, when the needle valve 48 is close to the entrance opening 36a of the small passage 36, the gap between the tip tip portion of the needle and the entrance opening 36a is a sharp portion. The air enters the small passage 36 with a stable flow and flows into the mixing chamber 40 side.

有機質廃液圧送管14は、前述したとおりの、焼酎廃液(焼酎滓)、大豆等の煮汁廃液その他の種々の食品加工工程で廃棄される廃液、豚、鶏、牛等の糞尿その他の畜産糞尿廃液その他の有機質系廃液(例えば含水率90%以上程度のもの)を圧送する管路手段であり、例えば合成樹脂あるいは金属管から構成するとよい。有機質系廃液圧送管14は廃液タンク60に接続され流量調整用のレギュレータ62を介して設定された流量の廃液が圧送される。廃液タンク60は種々の工程や事業所から排出される前処理後の有機系廃液の貯留タンクであり、コンプレッサからの空気圧供給管64を介してコンプレッサ66に接続されている。   As described above, the organic waste liquid pressure feed pipe 14 is a shochu waste liquid (shochu), a boiled liquid waste such as soybeans, a waste liquid discarded in various other food processing processes, a manure such as pigs, chickens and cattle, and other livestock manure waste liquids. It is a conduit means for pumping other organic waste liquid (for example, having a water content of about 90% or more), and may be composed of, for example, a synthetic resin or a metal pipe. The organic waste liquid pressure-feed pipe 14 is connected to a waste liquid tank 60 and the waste liquid having a flow rate set through a regulator 62 for flow rate adjustment is pressure-fed. The waste liquid tank 60 is a storage tank for pre-processed organic waste liquid discharged from various processes and offices, and is connected to a compressor 66 via an air pressure supply pipe 64 from the compressor.

助燃材圧送管16は、空気と有機系廃液とともに中空閉鎖容器内に圧送される助燃材を圧送する管路手段であり、流量調整用レギュレータ68を介して助燃材タンク70に接続されている。そして、助燃材タンク70は空気圧供給管64を介して廃液側に圧送力を供給駆動すると同じコンプレッサ66に接続されている。ここに、助燃材は、中空閉鎖容器内で空気と有機廃液とともに混合されて噴射ノズル20から微粒子状ミストとして外部に噴出される際の燃焼補助あるいは補助燃料手段であり、この微粒子状ミストに着火させた際に生ずる燃焼反応媒体の構成要素である。具体的には、例えば油類などの、水に不溶の可燃性の液体や、可燃性ガスなどを含む。より詳しくは、助燃材としては、例えば灯油、重油、軽油、ガソリン等の液体燃料や、天然ガス、液化石油ガス、都市ガス等の気体燃料を含む流体燃料である。好ましくは、家庭、飲食物提供業者、学校、事業所、その他の施設などから排出される食用油や古くなった食用油などの廃食油が資源のリサイクルと廃棄物量の削減を通じて環境保護にも資する点でよい。   The auxiliary combustion material pumping pipe 16 is a conduit means for pumping the auxiliary combustion material to be pumped into the hollow closed container together with air and organic waste liquid, and is connected to the auxiliary combustion material tank 70 via a flow rate adjusting regulator 68. The auxiliary combustion material tank 70 is connected to the same compressor 66 as the pressure feeding force is supplied to the waste liquid side via the air pressure supply pipe 64. Here, the auxiliary combustion material is combustion auxiliary or auxiliary fuel means when being mixed together with air and organic waste liquid in the hollow closed container and ejected to the outside as the particulate mist from the injection nozzle 20, and the particulate mist is ignited. It is a component of the combustion reaction medium generated when Specifically, for example, a flammable liquid insoluble in water, such as oils, or a flammable gas is included. More specifically, examples of the auxiliary combustion material include liquid fuels such as kerosene, heavy oil, light oil, and gasoline, and fluid fuels including gaseous fuels such as natural gas, liquefied petroleum gas, and city gas. Preferably, edible oil discharged from households, food and beverage providers, schools, business establishments, and other facilities contributes to environmental protection through resource recycling and waste reduction. That's fine.

コンプレッサ66は、少なくとも空気圧送管18に接続されて高圧空気を発生供給する空気圧発生駆動手段であり、本実施形態では流量計72を介設させた空気圧供給管64の一端側が連通接続されている。そして、4個の連通ポート34a〜34dにそれぞれ接続された空気圧送管18a〜18dは、N位置で相互に連通接続されており、このN位置に空気圧供給管64aの他端側が共通に連通するように接続されている。したがって、各連通ポート34a〜34dから同圧の空気が空気室38内に圧送供給される。さらに、本実施形態において、該コンプレッサ66には他の空気圧供給管64b、64cを介してそれぞれ廃液タンク60並びに助燃材タンク70にも連通接続しており、これによって、空気圧送管18、有機質廃液圧送管14ならびに助燃材圧送管16のそれぞれが同じ空気圧発生駆動手段に接続されて、略同空気圧力を加えて圧送する。これによって、混合室40内での圧力差による他のポートへの逆流を生じさせないとともに、略同圧の空気圧で空気室38内に圧送するから過度の高圧により小通路36から空気のみが噴出ノズルから噴出されて燃焼を生起させにくくすることなく、適切な微粒子ミストを発生させて燃焼を好適に維持させることができる。なお、空気圧送管18からの空気室38への圧力は、有機質廃液又は助燃材と同じかあるいはそれらよりも高い圧力で圧送される必要がある。空気圧送管18、有機質廃液圧送管14ならびに助燃材圧送管16からの圧力は少なくとも大気圧よりも高い圧力である必要がある。ただし、大気圧との関係で大幅に高圧で設定する必要はなく、連通ポート30〜34から閉鎖容器の中空部へのある程度の吐出力があればよい。好ましくは、圧力Pは1<P<10気圧程度であるとよい。10気圧以上の圧力とすると廃液、助燃材、空気量の空気室あるいは空気を受け入れた混合室での混合状態が微妙な圧力差で大きく変動するおそれが高く、燃焼に好ましい条件で噴出ノズルから噴出させるための設定を不必要に困難にするおそれがある。空気圧送管18、有機質廃液圧送管14ならびに助燃材圧送管16のそれぞれに同じ空気圧を供給するためには、必ずしもそれぞれの管が同じコンプレッサに接続されている必要はなく、別々の発生駆動手段により略同圧の設定により空気を圧送するようにしてもよい。   The compressor 66 is a pneumatic pressure generating drive unit connected to at least the pneumatic feeding pipe 18 to generate and supply high-pressure air. In this embodiment, one end side of a pneumatic supply pipe 64 provided with a flow meter 72 is connected in communication. . The pneumatic feed pipes 18a to 18d connected to the four communication ports 34a to 34d are connected to each other at the N position, and the other end side of the pneumatic supply pipe 64a is connected to the N position in common. So connected. Therefore, air of the same pressure is pressure-fed and supplied into the air chamber 38 from each of the communication ports 34 a to 34 d. Further, in the present embodiment, the compressor 66 is also connected to the waste liquid tank 60 and the auxiliary combustion material tank 70 via other pneumatic supply pipes 64b and 64c, respectively, whereby the pneumatic feed pipe 18 and the organic waste liquid are connected. Each of the pressure feeding pipe 14 and the auxiliary combustion material pressure feeding pipe 16 is connected to the same air pressure generation driving means, and is fed by applying substantially the same air pressure. As a result, a back flow to another port due to a pressure difference in the mixing chamber 40 is not generated, and air is pumped into the air chamber 38 with substantially the same air pressure, so that only air is ejected from the small passage 36 due to excessive high pressure. Therefore, it is possible to appropriately maintain the combustion by generating an appropriate fine particle mist without making it difficult to cause the combustion. In addition, the pressure to the air chamber 38 from the pneumatic feeding pipe 18 needs to be pumped at the same or higher pressure than the organic waste liquid or the auxiliary combustion material. The pressure from the pneumatic feeding pipe 18, the organic waste liquid feeding pipe 14 and the auxiliary combustion material feeding pipe 16 needs to be at least higher than the atmospheric pressure. However, it is not necessary to set a significantly high pressure in relation to the atmospheric pressure, and it is sufficient if there is a certain amount of discharge force from the communication ports 30 to 34 to the hollow portion of the closed container. Preferably, the pressure P is about 1 <P <10 atm. If the pressure is 10 atmospheres or more, there is a high possibility that the mixing state in the waste liquid, auxiliary material, air chamber of air volume or mixing chamber that receives air will greatly fluctuate due to a subtle pressure difference, and it is ejected from the ejection nozzle under conditions favorable for combustion. There is a risk of making the setting for making it unnecessarily difficult. In order to supply the same air pressure to the pneumatic feeding pipe 18, the organic waste liquid feeding pipe 14, and the auxiliary combustion material feeding pipe 16, the pipes do not necessarily have to be connected to the same compressor. Air may be pumped by setting substantially the same pressure.

これによって、燃焼ノズル装置10の噴出ノズル20近傍に着火装置22を配置し、発生する燃焼エネルギーを熱源又は動力源として利用することができる。この場合、図1における燃焼室150内の着火装置22による着火はそれに必要な程度の極めて弱いパイロットバーナでよく、したがって、燃料消費量もわずかの量である。   Thereby, the ignition device 22 can be arranged in the vicinity of the ejection nozzle 20 of the combustion nozzle device 10, and the generated combustion energy can be used as a heat source or a power source. In this case, the ignition by the ignition device 22 in the combustion chamber 150 in FIG. 1 may be an extremely weak pilot burner necessary for it, and the fuel consumption is also a small amount.

次に本実施形態の作用について図1、図3を主に参照して説明すると、例えば有機廃液を焼酎廃液とし、助燃材に廃食油を用いる場合、同圧発生装置としてのコンプレッサ66からの圧縮空気は空気圧供給管64a、64b、64cを介してそれぞれ空気室38及び混合室40に連通ポート30〜34を介して高圧で圧送される。この際、空気は流量計72、有機廃液及び助燃材は流量調整レギュレータ62,68によりそれぞれ流量を調節されて供給される。空気室38及び混合室40には略同圧の圧送力で空気、有機廃液、助燃材が同時に供給されており、それらの混合流体はすべて混合室40から噴出ノズル20を介して低圧の外部(外気)側へ噴出される。小通路36を介して空気室38から混合室40へ流入する空気量はニードル弁装置50を介して装置の外部から手動の摘み操作で可能となっている。小通路36から混合室側に出る空気は直線状の小通路により案内されて直線状かつビーム状となって混合室に流出しその流出方向のエネルギーを大幅に減殺されることなくオリフィス状出口20aから低圧大気側に微粒子状ミストが放出される。この際、混合室40内には空気流れ方向と直交、あるいは略直交方向から圧送される有機廃液及び助燃材と高速に混合される。図2のように、本実施形態では有機廃液と助燃材とは混合室内で同一直線上を対向方向から衝突するように供給され、相互にぶつかり合いながら混合し、さらにこれに直交方向から空気室からの空気が圧送される。これによって、噴出ノズルのオリフィス状出口20aの内側部分で大きな圧力となるとともに,この出口20aを出ると混合流体は一気に圧力を開放され、例えば120度の開き角に設定されたテーパ流路26の拡大壁に案内されて微粒子状ミストとして外部に拡大するように噴出される。この微粒子状ミストが燃材とされる。そして、噴出ノズルの先端近傍に予め設置したパイロットバーナ等の着火装置22を介して着火し、例えば燃焼室150内で燃焼する。上記のように、同時に同圧で圧入した有機廃液と助燃材と空気とを混合流体とし、この状態で外部に噴出させて微粒子状ミスト状態で着火させるから、有機廃液の特性、例えば粘度、繊維質成分や油分の多寡いかんにかかわらず基本的にどのような有機廃液も燃焼処理可能である。また、このため、廃棄物として環境負荷を増加させていたものを燃料の一部として機能させ、熱源あるいは動力源として駆動力を供給することができる。なお、廃食油と有機廃液との混合比は、体積比で例えば1:1から1:5程度の範囲であるとよく、廃食油のほうが有機廃液よりも少ないと安定した燃焼が得られにくい。   Next, the operation of the present embodiment will be described mainly with reference to FIG. 1 and FIG. 3. For example, when organic waste liquid is used as shochu waste liquid and waste cooking oil is used as the auxiliary combustion material, compression from the compressor 66 as the same pressure generator is performed. The air is pumped at a high pressure via the communication ports 30 to 34 to the air chamber 38 and the mixing chamber 40 through the air pressure supply pipes 64a, 64b and 64c, respectively. At this time, the air is supplied with the flow rate adjusted by the flow meter 72 and the organic waste liquid and the auxiliary combustion material are adjusted by the flow rate adjusting regulators 62 and 68, respectively. Air, organic waste liquid, and auxiliary combustion material are simultaneously supplied to the air chamber 38 and the mixing chamber 40 with a pumping force of substantially the same pressure. It is ejected to the outside air) side. The amount of air flowing from the air chamber 38 to the mixing chamber 40 via the small passage 36 can be manually picked from the outside of the device via the needle valve device 50. The air exiting from the small passage 36 toward the mixing chamber is guided by the straight small passage and flows out into the mixing chamber in the form of a straight line and a beam, and the orifice-shaped outlet 20a is not greatly reduced in the outflow direction. The fine mist is discharged from the low pressure atmosphere side. At this time, the mixing chamber 40 is mixed at high speed with the organic waste liquid and the auxiliary combustion material pumped from the direction perpendicular to or substantially perpendicular to the air flow direction. As shown in FIG. 2, in this embodiment, the organic waste liquid and the auxiliary combustion material are supplied so as to collide from the opposite direction on the same straight line in the mixing chamber, and are mixed while colliding with each other. Air from is pumped. As a result, a large pressure is generated at the inner portion of the orifice-shaped outlet 20a of the ejection nozzle, and the mixed fluid is released at once when exiting the outlet 20a. For example, the taper flow path 26 is set at an opening angle of 120 degrees. It is guided by the expansion wall and ejected to expand to the outside as fine particle mist. This particulate mist is used as a fuel. Then, it is ignited via an ignition device 22 such as a pilot burner installed in the vicinity of the tip of the ejection nozzle, and burns in, for example, the combustion chamber 150. As described above, the organic waste liquid, the auxiliary combustion material and the air simultaneously injected at the same pressure are mixed fluid, and in this state, the liquid is ejected to the outside and ignited in the form of fine mist, so the characteristics of the organic waste liquid such as viscosity, fiber, etc. Regardless of the quality component and the amount of oil, basically any organic waste liquid can be combusted. For this reason, what has increased environmental load as waste can be made to function as a part of fuel, and drive power can be supplied as a heat source or a power source. The mixing ratio of the waste cooking oil and the organic waste liquid is preferably in a range of, for example, about 1: 1 to 1: 5 by volume. If the waste cooking oil is less than the organic waste liquid, stable combustion is difficult to obtain.

なお、図5に示すように、有機廃液と助燃材とはすれ違い状に混合室内に流入するように各連通ポート30,32を混合室に連通接続させてもよく、例えば同圧空気を上流側の空気室から圧送して混合流体として噴出ノズルから外部に噴出させるようにするとよい。   As shown in FIG. 5, the communication ports 30 and 32 may be connected to the mixing chamber so that the organic waste liquid and the auxiliary combustion material flow into the mixing chamber so as to pass each other. It is preferable that the air is pumped from the air chamber and ejected from the ejection nozzle as a mixed fluid.

上記のような有機質系廃液の燃焼ノズル装置は、例えば図6に示すような熱源機器やエネルギー発生装置に連結接続させて熱源あるいは動力源として利用できる。例えば図6の例では、噴出ノズル20の近傍に着火装置22を配置した燃焼ノズル装置10に、タービンや発電機を接続し、工業用の各種動力源に用いることができる。また、ボイラや暖房あるいは蓄熱装置などに接続して、高温、高圧蒸気を発生させ、さらには熱交換等を介して室内空調機器への熱源機器として利用することができる。この場合、混合室40からは空気と有機廃液と助燃材との混合流体、特に助燃材を予め流体中に混合させた状態の微粒子ミスト状態で燃焼させるから、噴出ノズル先端からの着火装置による着火位置までの距離により燃焼効率を変動させる。すなわち、有機廃液には高粘度、あるいは粘度を有するものが多く、噴出の際の粒子の到達距離もそれぞれ異なる。したがって、燃焼物としてのこれらの廃液及び助燃材の到達位置付近が最も火力が強くなる。このため、有機廃液の種類あるいは使用する助燃材によって、ノズル先端から着火位置までの距離を可変設定するとよい。図9において、噴出ノズル20の前方近傍に着火位置可変機構74が設けられている。着火位置可変機構74は、トーチ部76と、燃焼雰囲気から離隔された位置に設置されたガス貯留用タンク78と、タンクを移動させる案内フレーム上を直線状に進退移動するスライダ80と、スライダとラック・ピニオン結合された伝達部82と、駆動モータ84と、を含む。モータ駆動力でスライダ80を移動させることにより、噴出ノズル20の先端位置からのトーチ部76による着火位置を可変設定し最適の燃焼条件で有機廃液を燃焼させる。特に、中空閉鎖容器に圧送する有機質廃液と助燃材との粘度に対応して噴出ノズルの先端からの着火位置を設定するとよい。   The organic waste liquid combustion nozzle device as described above can be used as a heat source or a power source by being connected to a heat source device or an energy generator as shown in FIG. For example, in the example of FIG. 6, a turbine or a generator can be connected to the combustion nozzle device 10 in which the ignition device 22 is disposed in the vicinity of the ejection nozzle 20 and used for various industrial power sources. Further, it can be connected to a boiler, heating or a heat storage device to generate high-temperature and high-pressure steam, and can be used as a heat source device for indoor air-conditioning equipment through heat exchange or the like. In this case, the mixing chamber 40 burns in a mixed fluid of air, organic waste liquid, and auxiliary combustion material, particularly in a fine particle mist state in which the auxiliary combustion material is previously mixed in the fluid. The combustion efficiency is changed depending on the distance to the position. That is, many organic waste liquids have high viscosity or viscosity, and the reach distance of particles at the time of ejection is different. Therefore, the thermal power becomes strongest in the vicinity of the position where these waste liquids and auxiliary combustion materials as combustion products arrive. Therefore, the distance from the nozzle tip to the ignition position may be variably set according to the type of organic waste liquid or the auxiliary combustion material used. In FIG. 9, an ignition position varying mechanism 74 is provided in the vicinity of the front of the ejection nozzle 20. The ignition position varying mechanism 74 includes a torch portion 76, a gas storage tank 78 installed at a position separated from the combustion atmosphere, a slider 80 that linearly moves back and forth on a guide frame that moves the tank, A transmission unit 82 coupled to a rack and pinion and a drive motor 84 are included. By moving the slider 80 by the motor driving force, the ignition position by the torch portion 76 from the tip position of the ejection nozzle 20 is variably set, and the organic waste liquid is burned under optimum combustion conditions. In particular, the ignition position from the tip of the ejection nozzle may be set according to the viscosity of the organic waste liquid and the auxiliary combustion material to be pumped to the hollow closed container.

次に、参考例について図7、8に基づき説明するが、前記した第1実施形態と同一部材には同一符号を付し、その詳細な説明は省略する。この参考例の有機質系廃液の燃焼ノズル装置11は、中空閉鎖容器12の中空部が空気室と混合室のように2分割されて連通された構造ではなく、閉鎖した一端壁側寄り位置から他端側の噴出ノズル20に連通する直状円柱形状の中空室86となっており、この中空室の円柱状空隙より少し小さな径で中空室の壁面との間に周状に連通する周状空隙88を形成するように円筒管90を収容させている。円筒管90の一端側は噴出ノズルの拡小テーパ流路28の入口部分に臨む位置に配置されるとともに、他端側は円柱状空隙の終端部との間に合流空隙92を形成するように終端部から少し控えた位置に設定してある。そして、この円筒管90の周方向複数個所には複数の空気注入孔94が穿孔されている。また、空隙88に連通するように空気圧送管に接続された4個の連通ポート34a〜34dが設けられている。連通ポート34a〜34dから圧送される圧縮空気は複数の空気注入孔94を介して円筒管90の内部に流入する。 Next, although a reference example is demonstrated based on FIG. 7, 8, the same code | symbol is attached | subjected to the same member as above-mentioned 1st Embodiment, and the detailed description is abbreviate | omitted. The organic waste liquid combustion nozzle device 11 of this reference example is not a structure in which the hollow portion of the hollow closed container 12 is divided and communicated in two, like an air chamber and a mixing chamber, but is different from a position close to one end wall side. It is a straight cylindrical hollow chamber 86 that communicates with the ejection nozzle 20 on the end side, and a circumferential void that communicates circumferentially with the wall surface of the hollow chamber with a slightly smaller diameter than the cylindrical void of this hollow chamber A cylindrical tube 90 is accommodated so as to form 88. One end side of the cylindrical tube 90 is disposed at a position facing the inlet portion of the enlarged taper flow path 28 of the ejection nozzle, and the other end side is formed with a joining gap 92 between the end of the cylindrical gap. The position is set slightly away from the end. A plurality of air injection holes 94 are formed at a plurality of locations in the circumferential direction of the cylindrical tube 90. In addition, four communication ports 34 a to 34 d connected to the pneumatic pipe so as to communicate with the gap 88 are provided. The compressed air fed from the communication ports 34 a to 34 d flows into the cylindrical tube 90 through the plurality of air injection holes 94.

また、合流空隙92に連通するように廃液圧送管としての第1連通ポート96、助燃材圧送管としての第2連通ポート98が本参考例ではY字状に該合流空隙92に連通するように形成されている。円筒管90の一端側開口は合流空隙92に臨んで連通しており、かつ、合流空隙92は円筒管90の中空内部にのみ連通するように形成されている。これによって、略同圧の圧送力で有機廃液と助燃材が同時に合流空隙92に圧送され、低圧側の装置外部側に向けて円筒管の中空部を通って噴出ノズル20側に流れる。有機廃液と助燃材が円筒管90内の中空部を直線状に流動する際、複数の空気注入孔94から圧縮空気が圧入され、これらの3つの要素が混合した混合流体の状態で噴出ノズル20側に至り、さらに、装置外部に微粒子状ミスとなって噴出される。なお、図9中、100は中空閉鎖容器本体と噴出ノズル20との組み付け接合時の気密用パッキン、102は、円筒管90と噴出ノズル内部側との接合気密パッキン、104は中空閉鎖容器本体と他端延長部との接合用気密パッキン、106は、他端延長部と円筒管90との組み付け接合時の気密パッキンである。 In addition, in this reference example , the first communication port 96 as the waste liquid pressure feeding pipe and the second communication port 98 as the auxiliary combustion material pressure feeding pipe communicate with the merging gap 92 in a Y shape so as to communicate with the merging gap 92. Is formed. One end side opening of the cylindrical tube 90 communicates with the joining gap 92, and the joining gap 92 is formed to communicate only with the hollow interior of the cylindrical tube 90. As a result, the organic waste liquid and the auxiliary combustion material are simultaneously pumped into the merged gap 92 with a pumping force of substantially the same pressure, and flow toward the ejection nozzle 20 through the hollow portion of the cylindrical tube toward the outside of the apparatus on the low pressure side. When the organic waste liquid and the auxiliary combustion material flow linearly through the hollow portion in the cylindrical tube 90, compressed air is injected from the plurality of air injection holes 94, and the ejection nozzle 20 is in a mixed fluid state in which these three elements are mixed. reaches the side, further, it is jetted become the particulate mist outside the apparatus. In FIG. 9, 100 is an airtight packing when the hollow closed container body and the ejection nozzle 20 are assembled and joined, 102 is an airtight packing between the cylindrical tube 90 and the inside of the ejection nozzle, and 104 is a hollow closed container body. An airtight packing for joining with the other end extension part 106 is an airtight packing when the other end extension part and the cylindrical tube 90 are assembled and joined.

なお、噴出ノズル20の構造に関し、図8に示すように最狭隘部分であるオリフィス状出口20aの手前の内部側入口部分を拡小テーパ流路とせずに、断面円弧状凹部としてもよい。   In addition, regarding the structure of the ejection nozzle 20, as shown in FIG. 8, the inner side inlet portion in front of the orifice-like outlet 20a, which is the narrowest narrow portion, may not be an enlarged tapered flow path but may be a concave portion having an arcuate cross section.

上記の参考例の有機質系廃液の燃焼ノズル装置においても、例えば図6に示すような熱源機器やエネルギー発生装置に連結接続させて熱源あるいは動力源として利用できることはもちろんである。また、燃焼対象や助燃材の粘度特性に応じた着火位置可変機構74を設置することもできる。 Of course, the organic waste liquid combustion nozzle apparatus of the above reference example can also be used as a heat source or a power source by being connected to, for example, a heat source device or an energy generator as shown in FIG. Moreover, the ignition position variable mechanism 74 according to the viscosity characteristic of a combustion object or auxiliary combustion material can also be installed.

上記のように、極めて小形の中空閉鎖容器内に略同圧で同時に異なる連通ポートを介して空気と、有機廃液と、助燃材とを圧送し、これを噴出ノズルから低圧側に向けて噴射する際の混合流体の微粒子状ミストの燃焼に関しては、実験的にも確認されている。   As described above, air, organic waste liquid, and auxiliary combustion material are pumped through an extremely small hollow closed container at the same pressure and simultaneously through different communication ports, and this is injected from the jet nozzle toward the low pressure side. The combustion of the particulate mist of the mixed fluid at that time has also been confirmed experimentally.

[実験例]焼酎廃液をメタン発酵して行なわれるメタンガス回収プロセスでの焼酎滓発酵残渣を有機廃液とし、助燃材としては廃食油を用いて図3の構成の燃焼ノズル装置による燃焼実験を行なった。図9は、その際の燃焼実験の概念構成図であり、噴出ノズルは横方向に向けて配置され、横方向に向けて混合流体が噴出される。噴出口からLの距離にパイロットバーナを設置して火種を作る。種火に到達した混合流体は火炎を形成し、その火炎挙動をデジタルビデオカメラで撮影し、パイロットバーナの位置及び焼酎廃液の発酵残渣と廃食油の比率を変化させ、火炎長さの変化を計測した。パイロットバーナの位置は噴射口からの距離Lで表し、火炎長さは最も火炎が長くなった瞬間のバーナ中心軸から火炎最長点までの距離λで表した。焼酎廃液発酵残渣と廃食油の比率が2:1、1:0、1:1、0:1、1:2の場合について行なった。さらに、各比率について、バーナ距離L[mm]を30,50,80,100,150,200及び250について行なった。
[結果と考察]火炎長さは図10に示すように、二つのパターンに分類できる。発酵残渣が廃食油よりも高い比率で含まれる場合と低い比率で含まれている場合である。発酵残渣の比率が高い場合、火炎はあまり発達しない。またバーナ距離が増大するにつれて火炎長さも増大した。一方廃食油の比率が高い場合や廃食油と発酵残渣の割合が同じ場合では、火炎は非常に発達し、バーナ距離は短いほうが火炎長さは長い。焼酎粕廃液の発酵残渣は粘度が低いため横方向に噴射した後、遠くまで液滴が飛散するが、廃食油は粘度が高いため飛距離が伸びない。したがって噴射口近くの噴霧には廃食油が多く含まれているが、噴射ノズルから離れると発酵残渣の比率が高くなる。以上の点から、噴射口付近には発熱量の高い廃食油が多量に含まれていて、火炎長さも長くなると思われる。以上より、噴霧は、ノズル噴射口から100〜150mm程度の位置において、焼酎廃液の発酵残渣と廃食油がよく混合されていることが分る。また、噴霧はノズル噴射口から50mm程度の位置で最もよく燃焼する。さらに、混合流体の発酵残渣と廃食油の割合は、同等か廃食油の割合を大きくしなければならない。但し、廃食油のみよりは発酵残渣が混合しているほうがよく燃焼することが分った。
[Experimental example] Combustion experiment was conducted with the combustion nozzle device shown in Fig. 3, using the residue of shochu fermentation in the methane gas recovery process performed by methane fermentation of the shochu waste liquor as organic waste liquor and waste cooking oil as the auxiliary combustion material. . FIG. 9 is a conceptual configuration diagram of a combustion experiment at that time. The ejection nozzle is arranged in the lateral direction, and the mixed fluid is ejected in the lateral direction. A pilot burner is installed at a distance L from the spout to create a fire. The mixed fluid that has reached the seed fire forms a flame, and the behavior of the flame is photographed with a digital video camera. The position of the pilot burner and the ratio of the fermentation residue and waste cooking oil in the shochu liquor are changed to measure the change in flame length. did. The position of the pilot burner is represented by a distance L from the injection port, and the flame length is represented by a distance λ from the burner central axis to the longest flame point at the moment when the flame becomes longest. The ratio of shochu liquor waste liquor fermentation residue to waste cooking oil was 2: 1, 1: 0, 1: 1, 0: 1, 1: 2. Furthermore, the burner distance L [mm] was performed for 30, 50, 80, 100, 150, 200, and 250 for each ratio.
[Results and Discussion] Flame lengths can be classified into two patterns as shown in FIG. It is the case where the fermentation residue is contained at a higher ratio than the waste cooking oil and at the lower ratio. If the proportion of fermentation residue is high, the flame does not develop much. The flame length also increased as the burner distance increased. On the other hand, when the ratio of waste cooking oil is high or when the ratio of waste cooking oil and fermentation residue is the same, the flame develops very much, and the shorter the burner distance, the longer the flame length. Since the fermentation residue of the shochu liquor has a low viscosity, the liquid droplets are scattered farther after being sprayed in the lateral direction. However, the waste cooking oil has a high viscosity, so the flight distance does not increase. Therefore, although a lot of waste cooking oil is contained in the spray near the injection port, the ratio of the fermentation residue increases as it moves away from the injection nozzle. From the above points, it is considered that a large amount of waste cooking oil with a high calorific value is contained in the vicinity of the injection port, and the flame length becomes long. From the above, it can be seen that in the spraying, the fermentation residue of the shochu waste liquid and the waste cooking oil are well mixed at a position of about 100 to 150 mm from the nozzle injection port. Further, the spray burns best at a position of about 50 mm from the nozzle injection port. Furthermore, the ratio of the fermentation residue and waste cooking oil of the mixed fluid must be equal or the ratio of waste cooking oil must be increased. However, it was found that the fermentation residue mixed better than the waste cooking oil alone.

本発明の有機質系廃液の燃焼ノズル装置、並びにエネルギー発生システムは、上記した実施形態の構成にのみ限られるものではなく、特許請求の範囲に記載した発明の本質を逸脱しない範囲における変更、改良も本発明に含まれる。   The organic waste liquid combustion nozzle device and the energy generation system of the present invention are not limited to the configuration of the above-described embodiment, and modifications and improvements within a scope not departing from the essence of the invention described in the claims are also possible. It is included in the present invention.

本発明の第1実施形態に係る有機質系廃液の燃焼ノズル装置を含む燃焼装置の概念構成説明図である。BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a conceptual configuration explanatory diagram of a combustion apparatus including an organic waste liquid combustion nozzle apparatus according to a first embodiment of the present invention. 第1実施形態に係る中空閉鎖容器の横断面図である。It is a cross-sectional view of the hollow enclosure according to the first embodiment. 第1実施形態に係る有機質系廃液の燃焼ノズル装置の縦断面説明図である。It is a longitudinal cross-sectional explanatory drawing of the combustion nozzle apparatus of the organic waste liquid which concerns on 1st Embodiment. 図3の有機質系廃液の燃焼ノズル装置の正面図である。It is a front view of the combustion nozzle apparatus of the organic waste liquid of FIG. 有機廃液及び助燃材と中空閉鎖容器との連通位置を異ならしめた中空閉鎖容器の横断面図である。It is a cross-sectional view of the hollow enclosure where the communication positions of the organic waste liquid and the auxiliary combustion material and the hollow enclosure are different. 本発明の有機質系廃液の燃焼ノズル装置を用いたエネルギー発生システムのブロック構成図である。It is a block block diagram of the energy generation system using the combustion nozzle apparatus of the organic waste liquid of this invention. 本発明の参考例に係る有機質系廃液の燃焼ノズル装置の縦断面説明図である。It is a longitudinal cross-sectional explanatory drawing of the combustion nozzle apparatus of the organic waste liquid which concerns on the reference example of this invention. 有機質系廃液の燃焼ノズル装置の噴出ノズル部分の他の例を示す要部拡大断面図である。It is a principal part expanded sectional view which shows the other example of the ejection nozzle part of the combustion nozzle apparatus of organic type waste liquid. 着火位置可変機構を含む実施形態概念図兼、燃焼実験の概念構成図である。It is an embodiment conceptual diagram including an ignition position variable mechanism and a conceptual configuration diagram of a combustion experiment. 実験例における噴出ノズル先端からトーチまでの距離Lと、トーチから火炎の先端までの距離λとの関係を示すグラフ図である。It is a graph which shows the relationship between the distance L from the ejection nozzle front-end | tip to a torch in an experiment example, and the distance (lambda) from a torch to the front-end | tip of a flame.

10 有機質系廃液の燃焼ノズル装置(第1実施形態)
12 中空閉鎖容器
14 有機質廃液圧送管
18a、18b、18c、18d 空気圧送管
20 噴出ノズル
22 着火手段
26 拡大テーパ流路
30 第1連通ポート
32 第2連通ポート
34a、34b、34c、34d 第3,4,5,6、連通ポート
36 小通路
38 空気室
40 混合室
50 ニードル弁装置
66 コンプレッサ
74 着火位置可変機構
96 第1連通ポート
98 第2連通ポート
110 燃焼装置
150 燃焼室
10. Combustion nozzle device for organic waste liquid (first embodiment)
12 Hollow closed vessel 14 Organic waste liquid pressure feeding pipe 18a, 18b, 18c, 18d Pneumatic feeding pipe 20 Jet nozzle 22 Ignition means 26 Expanded taper flow path 30 First communication port 32 Second communication port 34a, 34b, 34c, 34d Third, 4, 5, 6, communication port 36 small passage 38 air chamber 40 mixing chamber 50 needle valve device 66 compressor 74 ignition position variable mechanism 96 first communication port 98 second communication port 110 combustion device 150 combustion chamber

Claims (10)

中空閉鎖容器と、
中空閉鎖容器の中空部にそれぞれ異なる連通ポートで連通接続された有機質廃液圧送管と、助燃材圧送管と、空気圧送管と、
中空閉鎖容器内に圧送される有機質廃液と助燃材と空気との混合流体を大気側へ噴出させる噴出ノズルと、を含み、
有機質廃液と助燃材と空気とを同時に中空閉鎖容器内に圧送し噴出ノズルから噴出されるそれらの混合流体を燃材として着火燃焼させる有機質系廃液の燃焼ノズル装置であり、
空気圧送管の中空閉鎖容器との連通ポートは、有機質廃液と助燃材とのそれぞれの中空閉鎖容器との連通ポートよりも噴出ノズルに対して、より離隔した位置に設定されており、
さらに、中空閉鎖容器の中空部は、空気圧送管の連通ポートが連通する空気室と、有機質廃液圧送管と助燃材圧送管の各連通ポートが連通する混合室と、を小通路を中央にしてその両側に連通接続して設けられていることを特徴とする有機質系廃液の燃焼ノズル装置。
A hollow enclosure,
An organic waste liquid pressure feeding pipe, a combustible material pressure feeding pipe, a pneumatic feeding pipe, which are connected to the hollow portion of the hollow closed container through different communication ports,
A jet nozzle for jetting a mixed fluid of organic waste liquid, auxiliary combustion material and air pumped into the hollow closed container to the atmosphere side,
It is a combustion nozzle device for organic waste liquid that ignites and burns the mixed fluid ejected from the ejection nozzle as a fuel by simultaneously pumping the organic waste liquid, auxiliary combustion material and air into the hollow closed container,
The communication port with the hollow closed container of the pneumatic feeding pipe is set at a position farther away from the ejection nozzle than the communication port with each hollow closed container of the organic waste liquid and the auxiliary combustion material,
Further, the hollow portion of the hollow closed container has an air chamber that communicates with the communication port of the pneumatic feeding pipe, and a mixing chamber that communicates with each communication port of the organic waste liquid pressure feeding pipe and the auxiliary combustion material pressure feeding pipe, with a small passage at the center. A combustion nozzle device for organic waste liquid, wherein the combustion nozzle device is provided in communication with both sides .
小通路は、噴出ノズルのノズル孔の芯合わせ方向に長い通路からなる請求項記載の有機質系廃液の燃焼ノズル装置。 Small passage, combustion nozzle unit of organic-based waste of claim 1, wherein comprising a long passage in centering direction of the nozzle hole of the ejection nozzle. 小通路を介して空気室から混合室へ空気を圧送する際の空気の流量を調節する調節弁機構が設けられていることを特徴とする請求項1又は2記載の有機質系廃液の燃焼ノズル装置。 3. An organic waste liquid combustion nozzle device according to claim 1, further comprising a control valve mechanism for adjusting a flow rate of air when air is pumped from the air chamber to the mixing chamber through the small passage. . 調節弁機構は、ニードルの先端を小通路の入り開口に突入するように進退移動するニードル弁装置からなる請求項記載の有機質系廃液の燃焼ノズル装置。 4. A combustion nozzle device for organic waste liquid according to claim 3 , wherein the control valve mechanism comprises a needle valve device that moves forward and backward so that the tip of the needle enters the entrance of the small passage. すくなくとも有機質廃液圧送管と助燃材圧送管とは、同じ圧縮装置に連通されて有機質廃液と助燃材とが中空部に圧送されることを特徴とする請求項1ないしのいずれかに記載の有機質系廃液の燃焼ノズル装置。 The at least organic waste pumping pipe and improve combustion pumping tube, organic according to any one of claims 1 to 4 and organic waste and improve combustion in communication with the same compression apparatus is characterized in that it is pumped into the hollow portion System waste liquid combustion nozzle device. 少なくとも有機質廃液と助燃材とは略同じ圧送力で中空閉鎖容器内に圧送されることを特徴とする請求項1ないしのいずれかに記載の有機質系廃液の燃焼ノズル装置。 At least organic waste and organic-based waste combustion nozzle device according substantially to any claims 1, characterized in that it is pumped into the hollow closure vessel 5 with the same pumping power and improve combustion. 空気は有機質廃液又は助燃材と略同じかあるいはそれらよりも高い圧力で圧送されることを特徴とする請求項1ないしのいずれかに記載の有機質系廃液の燃焼ノズル装置。 Organic-based waste combustion nozzle device according to any one of air claims 1, characterized in that it is pumped at substantially the same or a higher pressure than those with organic waste or improve combustion 6. 中空閉鎖容器に圧送される助燃材と有機質廃液とが容積比で1:1〜5:1で設定されていることを特徴とする請求項1ないしのいずれかに記載の有機質系廃液の燃焼ノズル装置。 The combustion of the organic waste liquid according to any one of claims 1 to 7 , wherein the auxiliary combustion material and the organic waste liquid pumped to the hollow closed container are set at a volume ratio of 1: 1 to 5: 1. Nozzle device. 請求項1ないしのいずれかの燃焼ノズル装置の噴出ノズル近傍に着火装置を配置し、発生する燃焼エネルギーを熱源又は動力源として利用することを特徴とするエネルギー発生システム。 Energy generation system characterized by claims 1 to that place the ignition device in the vicinity jet nozzle of one of the combustion nozzle device 8 utilizes a combustion energy generated as a heat source or a power source. 中空閉鎖容器に圧送する有機質廃液と助燃材との粘度に対応して噴出ノズルの先端から着火装置による着火位置までの距離を変更設定する着火位置可変機構を有することを特徴とする請求項記載のエネルギー発生システム。 According to claim 9, characterized in that it has an ignition position varying mechanism for changing set the distance corresponding to the viscosity of the organic waste and improve combustion for pumping the hollow closed container from the tip of the jet nozzle to the ignition position by the ignition device Energy generation system.
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