JP4829617B2 - Method and apparatus for using waste cooking oil as fuel - Google Patents

Method and apparatus for using waste cooking oil as fuel Download PDF

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JP4829617B2
JP4829617B2 JP2006004921A JP2006004921A JP4829617B2 JP 4829617 B2 JP4829617 B2 JP 4829617B2 JP 2006004921 A JP2006004921 A JP 2006004921A JP 2006004921 A JP2006004921 A JP 2006004921A JP 4829617 B2 JP4829617 B2 JP 4829617B2
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oil
fuel
waste edible
edible oil
waste
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JP2007186574A (en
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和樹 小林
浩 石坂
郷紀 佐々木
健 広田
宣明 清水
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Mitsubishi Power Ltd
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Babcock Hitachi KK
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/10Biofuels, e.g. bio-diesel
    • 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
    • Y02TCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
    • Y02T10/00Road transport of goods or passengers
    • Y02T10/10Internal combustion engine [ICE] based vehicles
    • Y02T10/12Improving ICE efficiencies

Description

本発明はディーゼルエンジンに係り、特に廃食用油をディーゼルエンジンの燃料として利用する方法と装置に関する。   The present invention relates to a diesel engine, and more particularly to a method and apparatus for using waste edible oil as fuel for a diesel engine.

廃棄物問題、CO発生量の抑制等の環境問題の観点から、食品産業や家庭から排出される廃食用油をディーゼル燃料として再資源化する取り組みが行われている。廃食用油をディーゼル燃料として消費することで廃棄物処理の問題を緩和し、また燃焼によって発生したCOは再び菜の花によって吸収され、その菜の花から作られた食用油を食品加工等に使用した後の廃食用油をディーゼル燃料とするといった循環を形成することで、軽油、重油等の化石燃料を廃食用油で置換した量に相当するCOを削減することができる。 From the viewpoint of waste problems and environmental problems such as the reduction of CO 2 emissions, efforts are being made to recycle waste cooking oil discharged from the food industry and households as diesel fuel. After the waste cooking oil is consumed as diesel fuel, the problem of waste disposal is alleviated, and the CO 2 generated by combustion is absorbed by the rapeseed again, and the edible oil made from the rapeseed is used for food processing etc. By forming a circulation in which the waste edible oil is used as diesel fuel, CO 2 corresponding to the amount of fossil fuel such as light oil and heavy oil replaced with the waste edible oil can be reduced.

廃食用油をディーゼル燃料として利用する場合には、一旦エステル化処理を行って軽油相当の燃料に改質して使用される。この場合エステル化処理にコストがかかり、従来の燃料油と比較したときのコストメリットはわずかである。   When waste edible oil is used as diesel fuel, it is once used by being esterified and reformed into fuel equivalent to light oil. In this case, the esterification treatment is costly, and the cost merit when compared with conventional fuel oil is small.

別の改質法として特殊な装置を用いて高速攪拌する方法が特許文献1に提案されている。また、特許文献2には、廃食用油を加熱してフィルタで固形物を除去してディーゼルエンジンの燃料油とする技術が開示され、特許文献3には、廃食用油をヒータ、攪拌器を循環させ、燃焼装置の供給燃料とすることが開示されている。特許文献3にはまた、廃食用油を灯油、重油と混合させることも記載されている。   As another modification method, Patent Document 1 proposes a high-speed stirring method using a special apparatus. Patent Document 2 discloses a technique for heating waste edible oil and removing solids with a filter to make fuel oil for a diesel engine. Patent Document 3 discloses waste edible oil as a heater and stirrer. It is disclosed that it is circulated and used as a fuel supply for a combustion apparatus. Patent Document 3 also describes mixing waste cooking oil with kerosene and heavy oil.

特公昭58−273210号公報Japanese Patent Publication No.58-273210 特開平4−222311号公報JP-A-4-22211 特開昭64−000197号公報JP-A 64-000197

上記従来のエステル化処理技術には次のような問題点がある。リノール酸、リノレン酸等の不飽和脂肪酸を含有する廃食用油をディーゼル発電設備の燃料として使用する際に、これらの酸化や重合により生成するグリセリンなどがガム状物質となり、燃料フィルタの詰りの原因になっていた。   The above conventional esterification technology has the following problems. When waste edible oils containing unsaturated fatty acids such as linoleic acid and linolenic acid are used as fuel for diesel power generation facilities, the glycerin produced by oxidation and polymerization of these oils becomes a gum-like substance, which causes clogging of fuel filters It was.

また、これらガム状物質の生成は高温で促進され、噴射ポンプを燃料による冷却方式にしている新型エンジンの場合、燃料の循環過程の昇温でガム状物質が増加し、フィルタの詰りが加速される。   In addition, the generation of these gum-like substances is accelerated at high temperatures, and in the case of a new engine in which the injection pump is cooled by fuel, the gum-like substances increase as the temperature of the fuel circulation process increases, and filter clogging is accelerated. The

本発明の課題は、エステル化処理を行わない廃食用油をディーゼルエンジンの燃料として利用したときの長期の安定運転を可能にすることにある。   An object of the present invention is to enable long-term stable operation when waste edible oil that is not subjected to esterification is used as fuel for a diesel engine.

上記の課題は、廃食用油と重油を混合し、混合して得られた混合油を50℃〜120℃に加熱・昇温し、昇温された混合油にフィルタを通過させて高分子状の物質を含む不純物をろ過・除去し、ろ過後の混合油を燃料としてディーゼルエンジンに供給することにより、達成される。 The above problem is that waste edible oil and heavy oil are mixed, and the mixed oil obtained by mixing and heating is heated to a temperature of 50 ° C. to 120 ° C., and the heated mixed oil is passed through a filter to form a polymer. This is achieved by filtering and removing impurities containing these substances and supplying the filtered mixed oil as a fuel to a diesel engine.

廃食用油の混合、加熱・昇温に際しては、キャビテーションノズルを使用して廃食用油を重油に混合し、その際キャビテーションにより廃食用油を昇温させるよう構成してもよいし、混合油を燃料として利用するディーゼルエンジンの排気ガスの熱を利用して混合油を加熱・昇温するよう構成してもよい。 When mixing, heating and raising the temperature of waste edible oil, the edible edible oil may be mixed with heavy oil using a cavitation nozzle, and the temperature of the edible edible oil may be raised by cavitation. You may comprise so that mixed oil may be heated and heated using the heat | fever of the exhaust gas of the diesel engine utilized as a fuel.

また前記重油はA重油であることが望ましい。 The heavy oil is preferably A heavy oil.

上記の課題はまた、廃食用油と重油を混合し、混合油を生成する混合手段と、前記混合油を50℃〜120℃に加熱・昇温する昇温手段と、昇温された混合油から高分子状の物質を含む不純物をろ過・除去するろ過手段と、を有してなる廃食用油を燃料として利用する装置によっても達成される。 The above-mentioned problems also include a mixing means for mixing waste edible oil and heavy oil to produce a mixed oil, a temperature raising means for heating and raising the temperature of the mixed oil to 50 ° C. to 120 ° C. , and a heated mixed oil And a filtering means for filtering and removing impurities including a polymeric substance, and a device using waste edible oil as fuel.

前記昇温手段は、廃食用油を加圧する加圧手段と、加圧された廃食用油をキャビテーションジェットとして重油中に噴出するキャビテーションノズルと、を含んで構成してもよいし、混合油を燃料として利用するエンジンの排気ガスを熱源として混合油を加熱する熱交換器として構成してもよい。 The temperature raising unit may include a pressurizing unit that pressurizes the waste edible oil, and a cavitation nozzle that ejects the pressurized waste edible oil into the heavy oil as a cavitation jet. You may comprise as a heat exchanger which heats mixed oil by using the exhaust gas of the engine utilized as a fuel as a heat source.

図2に燃料油と廃食用油の混合油を加熱処理した際の、燃料油のフィルタろ過速度を未処理のものと比較して示す。横軸は処理量、縦軸はろ過に要した時間を示す。加熱処理したものはろ過速度が低下、すなわち、ろ紙の詰まりが早くなることを示している。未処理のものについても廃食用油中に不飽和脂肪酸由来と考えられる不純物があり、酸化や重合により粘性のあるグリセリンなどを生成、フィルタを詰まらせることになる。しかし、加熱処理により、不飽和脂肪酸の酸化、重合が促進され、高分子状のガム状物質が増加し、フィルタの目詰まり速度ははやくなる。   FIG. 2 shows the filter filtration rate of the fuel oil when the mixed oil of fuel oil and waste edible oil is heat-treated as compared with the untreated one. The horizontal axis indicates the amount of treatment, and the vertical axis indicates the time required for filtration. What was heat-processed has shown that the filtration rate falls, ie, clogging of filter paper becomes quick. Untreated food oil also contains impurities that are considered to be derived from unsaturated fatty acids in waste edible oil, which generates viscous glycerin and the like by oxidation and polymerization and clogs the filter. However, the heat treatment promotes the oxidation and polymerization of unsaturated fatty acids, increases the polymer-like gum substance, and speeds up the filter clogging.

図3に、一旦加熱したのちこれら不純物をろ過し、さらに再加熱した油をろ過したときのろ過速度と、初めて加熱した油のろ過速度の比較を示す。一旦加熱したのち、不純物をろ過すれば、その後再加熱してもろ過速度は変わらず(低下せず)、したがってフィルタ上にも不純物が残らないことがわかる。   FIG. 3 shows a comparison between the filtration rate when the impurities are filtered after heating once, and the reheated oil is filtered, and the filtration rate of the oil heated for the first time. It can be seen that once the impurities are filtered after heating, the filtration rate does not change (does not decrease) even after reheating, and therefore no impurities remain on the filter.

図4に同量の廃食用油を重油と混合する前に加熱したとき及び混合後に加熱したときの、ろ過速度、すなわち不純物の量を比較して示した。混合後加熱ろ過したものはろ過に要する時間が長い、つまりろ過速度の低下が早い。これは、A重油との混合により、A重油中の微量重金属の触媒作用で、前記重合反応が促進されたためであリ、廃食用油中の不純物を取り除くためには、混合後の加熱が望ましいことがわかる。   FIG. 4 shows a comparison of the filtration rate, that is, the amount of impurities when the same amount of waste edible oil is heated before mixing with heavy oil and when heated after mixing. A product that has been heated and filtered after mixing has a long time required for filtration, that is, the filtration rate decreases rapidly. This is because the polymerization reaction was promoted by the catalytic action of a trace amount of heavy metal in heavy oil A by mixing with heavy oil A. To remove impurities in waste cooking oil, heating after mixing is desirable. I understand that.

さらに、図5に示すように、A重油と廃食用油では、20℃における粘度が、A重油の5cStに対して廃食用油の90cSt程度と10倍以上差があり、廃食用油単独よりもA重油と混合後のほうが粘度が低下し、ハンドリングが容易になる。 また、廃食用油の混合にキャビテーションを利用し処理すると、混合時にキャビテーションジェットで廃食用油が昇温され、酸化が促進されるとともに、キャビテーションによる破壊効果で、グリセリンが分解される効果がある。   Furthermore, as shown in FIG. 5, in heavy oil A and waste edible oil, the viscosity at 20 ° C. is more than 10 times different from about 90 cSt of waste edible oil with respect to 5 cSt of heavy fuel oil A, compared with waste edible oil alone. After mixing with A heavy oil, the viscosity decreases and handling becomes easier. In addition, when cavitation is used for mixing the waste edible oil, the temperature of the waste edible oil is increased by a cavitation jet during mixing, and oxidation is promoted, and glycerin is decomposed due to the destructive effect of cavitation.

ディーゼルエンジンでは、燃料油は、燃料噴霧系を冷却するためにエンジンをポンプで循環され、その温度は50℃を越える。燃料油がこのような温度になるために高分子不純物の生成が促進され、エンジン内の燃料フィルタを閉塞させ、目詰まりを起こすことになる。   In a diesel engine, fuel oil is pumped through the engine to cool the fuel spray system and its temperature exceeds 50 ° C. Since the temperature of the fuel oil reaches such a temperature, the generation of polymer impurities is promoted, and the fuel filter in the engine is blocked and clogged.

事前に昇温して、フィルタろ過したものを実機に供給しても高温が保持されるわけではない。エンジンに供給された燃料油はエンジン内でポンプ冷却のために循環されるが、その温度は通常50℃になるものが、事前に昇温して、フィルタろ過したものを供給する場合60℃程度になるだけで、特に支障は無い。   Even if the temperature is raised in advance and the filtered product is supplied to the actual machine, the high temperature is not maintained. The fuel oil supplied to the engine is circulated in the engine for cooling the pump. The temperature is usually 50 ° C, but it is about 60 ° C when the preheated and filtered product is supplied. There is no particular problem.

本発明によれば、ディーゼルエンジンで燃料油と廃食用油の混合燃焼を行う際、フィルタの目詰まりが生じにくくなり、安定した運転が行われる期間が延長される効果がある。   According to the present invention, when mixed combustion of fuel oil and waste cooking oil is performed in a diesel engine, the filter is less likely to be clogged, and there is an effect that the period during which stable operation is performed is extended.

(第1の実施形態)
本発明をディーゼルエンジン発電装置に適用した第1の実施形態の構成を図1により説明する。本実施例に係るディーゼルエンジン発電装置は、燃料油タンク1と、廃食用油タンク2と、廃食用油と重油を混合する混合手段である混合セル7と、燃料油タンク1と混合セル7を接続する燃料油管18と、燃料油管18に介装された弁8及びポンプ9と、廃食用油タンク2と混合セル7を接続する廃食用油管19と、廃食用油管19に介装された弁8及びポンプ9と、混合セル7に混合油管21で接続されたディーゼルエンジン13と、混合油管21に上流側から順に介装された加熱・昇温手段である加熱装置12、ろ過手段であるフィルタユニット17及び弁22と、ディーゼルエンジン13で駆動される発電機14と、ディーゼルエンジン13の排ガスダクト23に設置された排ガス処理装置15と、を含んで構成されている。
(First embodiment)
A configuration of a first embodiment in which the present invention is applied to a diesel engine power generator will be described with reference to FIG. The diesel engine power generator according to this embodiment includes a fuel oil tank 1, a waste edible oil tank 2, a mixing cell 7 that is a mixing means for mixing waste edible oil and heavy oil, a fuel oil tank 1 and a mixing cell 7. A fuel oil pipe 18 to be connected, a valve 8 and a pump 9 interposed in the fuel oil pipe 18, a waste edible oil pipe 19 connecting the waste edible oil tank 2 and the mixing cell 7, and a valve interposed in the waste edible oil pipe 19 8, a pump 9, a diesel engine 13 connected to the mixing cell 7 with a mixed oil pipe 21, a heating device 12 as heating / heating means interposed in order from the upstream side into the mixed oil pipe 21, and a filter as filtering means The unit 17 and the valve 22, the generator 14 driven by the diesel engine 13, and the exhaust gas treatment device 15 installed in the exhaust gas duct 23 of the diesel engine 13 are configured.

図1の実施例において、混合セル7で燃料油と廃食用油を混合して生成された混合油は加熱装置12で約80℃に昇温され、高分子状の物質の生成が促進される。その後、不純物を除去するフィルタユニット17で高分子状の物質が除去され、燃料11としてディーゼルエンジン13へ供給される。ディーゼルエンジン13は供給された燃料を燃焼させて発電し、エンジン排ガスはフィルタを含む排ガス処理装置15で処理されたのち、排気16となって大気に放出される。   In the embodiment of FIG. 1, the mixed oil produced by mixing the fuel oil and the waste edible oil in the mixing cell 7 is heated to about 80 ° C. by the heating device 12, and the production of the polymer substance is promoted. . Thereafter, the polymer substance is removed by the filter unit 17 for removing impurities, and the fuel 11 is supplied to the diesel engine 13. The diesel engine 13 generates electric power by burning the supplied fuel, and the engine exhaust gas is processed by an exhaust gas processing device 15 including a filter, and then discharged into the atmosphere as exhaust 16.

本実施例では、混合油は加熱装置12で約80℃に昇温されるが、発明者らが確認したところでは、高分子状の物質の生成を促進するには、少なくとも50℃に昇温されることが望ましい。また、不飽和脂肪酸の気化防止のため、120℃以下とするのが望ましい。   In this embodiment, the mixed oil is heated to about 80 ° C. by the heating device 12, but the inventors have confirmed that the temperature of the mixed oil is increased to at least 50 ° C. in order to promote the formation of a polymer substance. It is desirable that Moreover, it is desirable to set it as 120 degrees C or less in order to prevent vaporization of unsaturated fatty acid.

本実施例によれば、燃料油と廃食用油を混合し、これを一旦昇温して高分子状の物質の生成を促進し、生成された高分子状の物質などの固形分をフィルタユニット17でろ過してからディーゼルエンジン13に供給するので、エンジン内でのフィルタ目詰まりは防止でき、2000h以上安定運転が可能になった。燃料11はエンジン内を循環して燃料噴霧系を冷却するので冷却による燃料11の昇温が生じる。しかし、事前に加熱装置12で昇温されフィルタユニット17でろ過されているので、冷却による燃料11の昇温が生じても新たな高分子状の物質の生成はなく、エンジン内でのフィルタ目詰まりは生じない。また、燃料油と廃食用油を混合したのち昇温するので、燃料油(重油)に含まれる微量重金属の触媒作用で不飽和脂肪酸由来の不純物の重合が促進される効果がある。   According to the present embodiment, fuel oil and waste edible oil are mixed, the temperature is once raised to promote the generation of a polymeric substance, and the solid content such as the generated polymeric substance is filtered out. Since it is supplied to the diesel engine 13 after being filtered at 17, the filter clogging in the engine can be prevented, and stable operation for 2000 hours or more is possible. Since the fuel 11 circulates in the engine and cools the fuel spray system, the temperature of the fuel 11 rises due to cooling. However, since the temperature is raised in advance by the heating device 12 and filtered by the filter unit 17, no new polymer substance is generated even when the temperature of the fuel 11 rises due to cooling, and the filter in the engine There is no clogging. Further, since the temperature is raised after mixing the fuel oil and the waste edible oil, there is an effect that the polymerization of impurities derived from the unsaturated fatty acid is promoted by the catalytic action of the trace heavy metal contained in the fuel oil (heavy oil).

(第2の実施形態)
本発明による第2の実施形態の構成を、図6を参照して説明する。図6に示す第2の実施形態のディーゼルエンジン発電装置が図1に示す前記第1の実施形態と異なる点は、廃食用油管19には、弁8とポンプ9に代えて圧縮ポンプ3と圧力調整弁4が介装され、混合セル7は廃食用油と重油を混合するキャビテーションノズル5を具備し、混合油管21には加熱装置12が介装されていない点である。廃食用油管19はキャビテーションノズル5を介して混合セル7に接続されている。キャビテーションノズル5には圧力計6が設けられている。他の構成は前記第1の実施形態と同じであるので同一の符号を付して説明を省略する。
(Second Embodiment)
The configuration of the second embodiment according to the present invention will be described with reference to FIG. The diesel engine power generator of the second embodiment shown in FIG. 6 is different from the first embodiment shown in FIG. 1 in that the waste edible oil pipe 19 has a compression pump 3 and a pressure instead of the valve 8 and the pump 9. The adjustment valve 4 is interposed, the mixing cell 7 includes a cavitation nozzle 5 for mixing waste cooking oil and heavy oil, and the heating device 12 is not interposed in the mixed oil pipe 21. The waste edible oil pipe 19 is connected to the mixing cell 7 via the cavitation nozzle 5. The cavitation nozzle 5 is provided with a pressure gauge 6. Since other configurations are the same as those of the first embodiment, the same reference numerals are given and description thereof is omitted.

本実施例においては、混合手段は混合セル7とキャビテーションノズル5で構成され、加熱・昇温手段は、加圧手段である圧縮ポンプ3と圧力調整弁4とキャビテーションノズル5を含んで構成されている。キャビテーションノズル5は加圧・昇温手段と混合手段を兼ねている。   In this embodiment, the mixing means is composed of a mixing cell 7 and a cavitation nozzle 5, and the heating / temperature raising means is composed of a compression pump 3, a pressure regulating valve 4 and a cavitation nozzle 5 that are pressurizing means. Yes. The cavitation nozzle 5 serves as a pressurizing / heating unit and a mixing unit.

廃食用油タンク2の廃食用油は圧縮ポンプ3で加圧され、圧力調整弁4を介して、キャビテーションノズル5に導入される。キャビテーションノズル5に導入された廃食用油は、燃料油が供給されている混合セル7内に高圧噴射され、キャビテーションジェット10を生じさせる。廃食用油はキャビテーションにより昇温されて燃料油と混合され、高分子状の物質の生成が促進される。高分子状の物質等の不純物を含む混合油はフィルタユニット17で高分子状の物質等の不純物をろ過されたのち、燃料11としてディーゼルエンジン13へ供給される。燃料11はエンジン内を循環して燃料噴霧系を冷却するので冷却による燃料11の昇温が生じる。しかし、事前にフィルタユニット17でろ過されているので、冷却による燃料11の昇温が生じても新たな高分子状の物質の生成はなく、エンジン内でのフィルタ目詰まりは生じない。ディーゼルエンジン13は供給された燃料を燃焼させて発電し、エンジン排ガスはフィルタを含む排ガス処理装置15で処理されたのち、排気16となって大気に放出される。これによりエンジン内でのフィルタ目詰まりは防止でき、2000h以上安定運転が可能になった。   Waste cooking oil in the waste cooking oil tank 2 is pressurized by the compression pump 3 and introduced into the cavitation nozzle 5 through the pressure regulating valve 4. Waste edible oil introduced into the cavitation nozzle 5 is injected at a high pressure into the mixing cell 7 to which fuel oil is supplied, thereby generating a cavitation jet 10. Waste edible oil is heated by cavitation and mixed with fuel oil to promote the production of a polymeric substance. The mixed oil containing impurities such as a polymer substance is filtered by the filter unit 17 and then supplied to the diesel engine 13 as the fuel 11. Since the fuel 11 circulates in the engine and cools the fuel spray system, the temperature of the fuel 11 rises due to cooling. However, since it has been filtered by the filter unit 17 in advance, even if the temperature of the fuel 11 rises due to cooling, no new polymer substance is generated, and the filter is not clogged in the engine. The diesel engine 13 generates electric power by burning the supplied fuel, and the engine exhaust gas is processed by an exhaust gas processing device 15 including a filter, and then discharged into the atmosphere as exhaust 16. As a result, filter clogging in the engine can be prevented, and stable operation for 2000 hours or more has become possible.

(第3の実施形態)
本発明の第3の実施形態の構成を、図7を参照して説明する。図7に示す第3の実施形態のディーゼルエンジン発電装置が図1に示す前記第1の実施形態と異なる点は、排ガス処理装置15の上流側の排ガスダクト23に熱回収熱交換器24が介装され、加熱装置12に代えて熱交換器20が混合油管21に介装されている点である。熱交換器20は熱回収熱交換器24に熱媒体流路で接続されており、加熱流体側流路を熱回収熱交換器24で熱回収して昇温された熱媒体が流れ、被加熱流体流路を混合セル7で混合生成された混合油が流れるように構成されている。他の構成は前記第1の実施形態と同じであるので同一の符号を付して説明を省略する。
(Third embodiment)
The configuration of the third embodiment of the present invention will be described with reference to FIG. The diesel engine power generation device of the third embodiment shown in FIG. 7 is different from the first embodiment shown in FIG. 1 in that a heat recovery heat exchanger 24 is interposed in the exhaust gas duct 23 on the upstream side of the exhaust gas treatment device 15. The heat exchanger 20 is interposed in the mixed oil pipe 21 instead of the heating device 12. The heat exchanger 20 is connected to the heat recovery heat exchanger 24 through a heat medium flow path, and the heat medium heated by heat recovery from the heat recovery heat exchanger 24 flows through the heating fluid side flow path, and is heated. The mixed oil produced and mixed in the mixing cell 7 flows through the fluid flow path. Since other configurations are the same as those of the first embodiment, the same reference numerals are given and description thereof is omitted.

本実施例においては、混合セル7で混合生成された混合油は排ガスを熱源に利用した熱交換器20で昇温され、高分子状の物質の生成が促進される。図示の実施例では、熱回収の位置は排ガス処理装置15の上流側としているが、混合油の昇温温度は80℃程度なので、排ガス処理装置下流側で熱回収しても問題ない。高分子状の物質の生成が促進された混合油は、不純物を除去するフィルタユニット17に導かれて高分子状の物質等の固形分が除去され、燃料11としてディーゼルエンジン13へ供給される。ディーゼルエンジン13は供給された燃料を燃焼させて発電し、エンジン排ガスは熱回収熱交換器24で熱回収された後、フィルタを含む排ガス処理装置15で処理され、排気16となって大気に放出される。これによりエンジン内でのフィルタ目詰まりは防止でき、2000h以上安定運転が可能になった。   In this embodiment, the mixed oil mixed and generated in the mixing cell 7 is heated by the heat exchanger 20 using the exhaust gas as a heat source, and the generation of a polymer substance is promoted. In the illustrated embodiment, the heat recovery position is on the upstream side of the exhaust gas treatment device 15, but since the temperature rise of the mixed oil is about 80 ° C., there is no problem even if heat recovery is performed on the downstream side of the exhaust gas treatment device. The mixed oil in which the generation of the polymer substance is promoted is guided to the filter unit 17 that removes impurities, and solids such as the polymer substance are removed and supplied to the diesel engine 13 as the fuel 11. The diesel engine 13 burns the supplied fuel to generate electricity, and the engine exhaust gas is recovered by the heat recovery heat exchanger 24 and then processed by the exhaust gas treatment device 15 including a filter to be discharged into the atmosphere as exhaust 16. Is done. As a result, filter clogging in the engine can be prevented, and stable operation for 2000 hours or more has become possible.

なお、上記各実施例におけるフィルタユニット17は、それぞれフィルタを備えた複数の流路を有し、各流路を系統から隔離できるようにしてある。したがって、所定の時間ごとに各流路を順次系統から切り離してフィルタの交換することで、エンジンへの混合油の供給を中断することがないようにしてある。   The filter unit 17 in each of the above embodiments has a plurality of flow paths each provided with a filter so that each flow path can be isolated from the system. Therefore, the supply of the mixed oil to the engine is not interrupted by sequentially disconnecting each flow path from the system and replacing the filter every predetermined time.

(比較例)
比較例を図8に示す。図8に示す比較例のディーゼルエンジン発電装置が図6に示す第2の実施形態と異なるのは、フィルタユニット17が設けられていない点である。他の構成は前記第2の実施形態と同じであるので同一の符号を付して説明を省略する。
(Comparative example)
A comparative example is shown in FIG. The diesel engine power generation device of the comparative example shown in FIG. 8 is different from the second embodiment shown in FIG. 6 in that the filter unit 17 is not provided. Since other configurations are the same as those of the second embodiment, the same reference numerals are given and description thereof is omitted.

この場合、廃食用油タンク2の廃食用油は圧縮ポンプ3で加圧され、圧力調整弁4を介して、キャビテーションノズル5に導入される。キャビテーションノズル5に導入された廃食用油は、燃料油が供給されている混合セル7内に高圧噴射され、キャビテーションジェット10を生じさせる。キャビテーションにより昇温された廃食用油は燃料油と混合されて高分子状の不純物を生成するが、フィルタユニット17が設けられていないので、生成された混合油は高分子状の不純物を含んだまま、燃料11としてディーゼルエンジン13へ供給される。燃料油はエンジン内でポンプ冷却のために循環され、その温度は50℃を越える。これにより、燃料11内に含まれている高分子不純物の生成が促進され、エンジン内のフィルタを閉塞、およそ50hで目詰まりを起こした。   In this case, the waste edible oil in the waste edible oil tank 2 is pressurized by the compression pump 3 and introduced into the cavitation nozzle 5 via the pressure adjustment valve 4. Waste edible oil introduced into the cavitation nozzle 5 is injected at a high pressure into the mixing cell 7 to which fuel oil is supplied, thereby generating a cavitation jet 10. The waste edible oil heated by cavitation is mixed with fuel oil to produce polymer impurities, but since the filter unit 17 is not provided, the produced mixed oil contains polymer impurities. The fuel 11 is supplied to the diesel engine 13 as it is. Fuel oil is circulated in the engine for pump cooling, and its temperature exceeds 50 ° C. As a result, the generation of polymer impurities contained in the fuel 11 was promoted, the filter in the engine was blocked, and clogging occurred in about 50 hours.

本発明の第1の実施形態のディーゼル発電装置の構成を示す系統図である。It is a distribution diagram showing the composition of the diesel power generator of a 1st embodiment of the present invention. 加熱処理を行った混合油と加熱処理を行っていない混合油のろ過速度を比較して示すグラフである。It is a graph which compares and shows the filtration rate of the mixed oil which heat-processed, and the mixed oil which has not heat-processed. 混合油を加熱後ろ過する場合とそれを更に再加熱後ろ過する場合の、ろ過に要する時間を比較して示すグラフである。It is a graph which compares and shows the time required for filtration when the mixed oil is filtered after heating and when it is further filtered after reheating. A重油と廃食用油を混合する前に加熱した場合と混合後に加熱した場合の、ろ過に要する時間を比較して示すグラフである。It is a graph which compares and shows the time required for filtration when heating before mixing A heavy oil and waste edible oil, and when heating after mixing. A重油、廃食用油、A重油と廃食用油を混合した混合油の3種の油それぞれについて、温度と粘度の関係を示すグラフである。It is a graph which shows the relationship between temperature and a viscosity about each of three types of oil of A heavy oil, waste edible oil, and mixed oil which mixed A heavy oil and waste edible oil. 本発明の第2の実施形態のディーゼル発電装置の構成を示す系統図である。It is a systematic diagram which shows the structure of the diesel electric power generating apparatus of the 2nd Embodiment of this invention. 本発明の第3の実施形態のディーゼル発電装置の構成を示す系統図である。It is a systematic diagram which shows the structure of the diesel electric power generating apparatus of the 3rd Embodiment of this invention. 比較例のディーゼル発電装置の構成を示す系統図である。It is a systematic diagram which shows the structure of the diesel generator of a comparative example.

符号の説明Explanation of symbols

1 燃料油タンク
2 廃食用油タンク
3 圧縮ポンプ
4 圧力調整弁
5 キャビテーションノズル
6 圧力計
7 混合セル
8 弁
9 ポンプ
10 キャビテーションジェット
11 燃料
12 加熱装置
13 ディーゼルエンジン
14 発電機
15 排ガス処理装置
16 排気
17 フィルタユニット
18 燃料油管
19 廃食用油管
20 熱交換器
21 混合油管
22 弁
23 排ガスダクト
24 熱回収熱交換器
DESCRIPTION OF SYMBOLS 1 Fuel oil tank 2 Waste cooking oil tank 3 Compression pump 4 Pressure control valve 5 Cavitation nozzle 6 Pressure gauge 7 Mixing cell 8 Valve 9 Pump 10 Cavitation jet 11 Fuel 12 Heating device 13 Diesel engine 14 Generator 15 Exhaust gas treatment device 16 Exhaust 17 Filter unit 18 Fuel oil pipe 19 Waste cooking oil pipe 20 Heat exchanger 21 Mixed oil pipe 22 Valve 23 Exhaust gas duct 24 Heat recovery heat exchanger

Claims (8)

廃食用油と重油を混合する混合手順と、混合して得られた混合油を50℃〜120℃に加熱・昇温する加熱・昇温手順と、昇温された混合油をフィルタでろ過して高分子状の物質を含む不純物を除去するろ過手順と、ろ過後の混合油を燃料としてディーゼルエンジンに供給する供給手順と、を有してなる、廃食用油を燃料として利用する方法。 Mixing procedure for mixing waste cooking oil and heavy oil, heating / heating procedure for heating / heating the mixed oil obtained by mixing to 50 ° C to 120 ° C , and filtering the heated mixed oil with a filter A method of using waste edible oil as a fuel, comprising: a filtration procedure for removing impurities including a polymeric substance; and a supply procedure for supplying the filtered mixed oil to a diesel engine as a fuel. 請求項1記載の廃食用油を燃料として利用する方法において、廃食用油の混合手順、加熱・昇温手順は、廃食用油を加圧し、キャビテーションノズルを使用して加圧された廃食用油を重油に混合し、その際キャビテーションにより廃食用油を昇温させるよう構成されていることを特徴とする廃食用油を燃料として利用する方法。 The method of using waste edible oil according to claim 1 as a fuel, wherein the waste edible oil mixing procedure and heating / heating step are performed by pressurizing the waste edible oil and pressurizing it using a cavitation nozzle. A method of using waste edible oil as fuel, characterized in that waste oil is mixed with heavy oil and the temperature of waste edible oil is raised by cavitation. 請求項1記載の廃食用油を燃料として利用する方法において、前記加熱・昇温手順は、混合油を燃料として利用するディーゼルエンジンの排気ガスの熱を利用して混合油を加熱・昇温するよう構成されていることを特徴とする廃食用油を燃料として利用する方法。   2. The method of using waste edible oil as fuel according to claim 1, wherein the heating / heating step uses the heat of exhaust gas from a diesel engine that uses the mixed oil as a fuel to heat / heat the mixed oil. A method of using waste edible oil as fuel characterized by being configured as described above. 請求項1〜のうちのいずれか1項記載の廃食用油を燃料として利用する方法において、前記重油はA重油であることを特徴とする廃食用油を燃料として利用する方法。 4. The method of using waste edible oil as fuel, wherein the heavy oil is A heavy oil , wherein the waste edible oil according to any one of claims 1 to 3 is used as fuel. 廃食用油と重油を混合し、混合油を生成する混合手段と、前記混合油を50℃〜120℃に加熱・昇温する昇温手段と、昇温された混合油から高分子状の物質を含む不純物をろ過・除去するろ過手段と、を有してなる廃食用油を燃料として利用する装置。 Mixing means for mixing waste cooking oil and heavy oil to produce mixed oil, heating means for heating / heating the mixed oil to 50 ° C. to 120 ° C. , and polymer substance from the heated mixed oil And a means for filtering / removing impurities that contain waste edible oil as fuel. 請求項記載の廃食用油を燃料として利用する装置において、前記昇温手段は、廃食用油を加圧する加圧手段と、加圧された廃食用油をキャビテーションジェットとして重油中に噴出するキャビテーションノズルと、を含んで構成されていることを特徴とする廃食用油を燃料として利用する装置。 6. The apparatus for using waste edible oil as fuel according to claim 5 , wherein the temperature raising means includes a pressurizing means for pressurizing the waste edible oil, and a cavitation jetting the pressurized waste edible oil into the heavy oil as a cavitation jet. A device using waste edible oil as fuel, characterized in that it comprises a nozzle. 請求項記載の廃食用油を燃料として利用する装置において、前記昇温手段は、混合油を燃料として利用するエンジンの排気ガスを熱源として混合油を加熱する熱交換器であることを特徴とする廃食用油を燃料として利用する装置。 6. The apparatus for using waste edible oil as fuel according to claim 5 , wherein the temperature raising means is a heat exchanger that heats the mixed oil by using an exhaust gas of an engine that uses the mixed oil as a fuel as a heat source. Equipment that uses waste cooking oil as fuel. 請求項5〜7のうちのいずれか1項記載の廃食用油を燃料として利用する装置において、前記重油がA重油であることを特徴とする廃食用油を燃料として利用する装置。 The apparatus which uses the waste edible oil as a fuel in the apparatus which uses the waste edible oil of any one of Claims 5-7 as a fuel, The said heavy oil is A heavy oil.
JP2006004921A 2006-01-12 2006-01-12 Method and apparatus for using waste cooking oil as fuel Expired - Fee Related JP4829617B2 (en)

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