JPS638483A - Regenerated fuel oil - Google Patents

Regenerated fuel oil

Info

Publication number
JPS638483A
JPS638483A JP15206086A JP15206086A JPS638483A JP S638483 A JPS638483 A JP S638483A JP 15206086 A JP15206086 A JP 15206086A JP 15206086 A JP15206086 A JP 15206086A JP S638483 A JPS638483 A JP S638483A
Authority
JP
Japan
Prior art keywords
oil
fuel
fuel oil
mixed
parts
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP15206086A
Other languages
Japanese (ja)
Inventor
Masasuke Kusaki
草木 荘輔
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Priority to JP15206086A priority Critical patent/JPS638483A/en
Publication of JPS638483A publication Critical patent/JPS638483A/en
Pending legal-status Critical Current

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Abstract

PURPOSE:Regenerated fuel oil, suitable as a heavy oil alternate fuel for boilers, etc., obtained by blending a used vegetable oil with a mineral oil having a specific boiling point in a specific amount. CONSTITUTION:100pts.vol. used vegetable oil of frying oil, salad oil, etc., is blended with 25-35pts.vol. mineral oil (preferably kerosene) having 35-250 deg.C boiling point to give the aimed fuel oil.

Description

【発明の詳細な説明】 (産業上の利用分野) 本ffi明は再生燃料油に関し、更に詳しくは使用済の
植物油と沸点が所定範囲の鉱油とを、ある割合で混合し
、これによって例えばボイラー等に重油に代わる燃料油
として使用できるようにした++f生燃料油に関するも
のである。
Detailed Description of the Invention (Field of Industrial Application) The present invention relates to recycled fuel oil, and more specifically, it is a method of mixing used vegetable oil and mineral oil with a boiling point within a certain range in a certain ratio, thereby producing a fuel oil that can be used in boilers, for example. The present invention relates to ++F raw fuel oil that can be used as a fuel oil in place of heavy oil, etc.

(従来技術とその問題点) 従来、使用済のいわゆる天ぷら油やサラダ油等の植物油
は、廃油として回収業者によって下取りされて、石鹸等
の=−二次製品に11f加丁されて使用されることが多
かった。しかしながらこのような1;1生使用は1回収
業者及び石鹸5A造業者両者の採算コストが見合う場合
にのみ可染であったから、例えば回収業者は、回収作業
が採算に合わなければ回収作業を行わなかったものであ
る。従って廃油を大、L7tに出す例えば給食センター
等の施設では、このような場合、廃油の処分に関して問
題が生じたものである。即ち、廃油を海−1:に投棄す
る場合には、海水汚染を招き、漁業被害の一因にもなる
という151題があり、又凝固剤を廃油に混入して廃油
を固化した後、一般のゴミと同様の廃棄処分をする場合
には、凝固剤の用意、混入という経済ヒ、労カヒの煩わ
しさが派生したものであった。
(Prior art and its problems) Conventionally, used vegetable oils such as tempura oil and salad oil are traded in as waste oil by collection companies and used after being added to secondary products such as soap. There were many. However, such 1:1 raw use was dyeable only if the profitability costs for both the 1 collection company and the soap 5A manufacturer were commensurate with each other, so for example, the collection company would carry out the collection work if it was not profitable. It's something that didn't exist. Therefore, in facilities such as school lunch centers that dispose of waste oil in large volumes, problems have arisen regarding the disposal of the waste oil in such cases. In other words, when waste oil is dumped into the sea, there are 151 problems, such as causing seawater pollution and contributing to damage to fisheries.Also, after solidifying the waste oil by mixing a coagulant into the waste oil, it is generally If they were to be disposed of in the same manner as other garbage, the economical and labor costs of preparing and mixing coagulants resulted.

而して廃油中には、水分を始めとする不純物の混入率が
高く、又酸化の度合が極めて高いだけではなく、引火点
も例えばいわゆる天ぷら油では通常250℃位であるこ
とから、そのまま例えば重油の代持燃料としてボイラー
等の燃料源に使用することもできなかったものである。
Waste oil has a high rate of contamination with water and other impurities, and is not only highly oxidized, but also has a flash point of, for example, tempura oil, which is usually around 250°C. It could not be used as a fuel source for boilers, etc. as a substitute fuel for heavy oil.

又この種の廃油に例えばガソリンをブレンドして、燃ネ
1油としての再利用を図る場合には、+lT生した燃キ
1油の容j−ちりの巾価と、燃料油としての有効性との
調整が特に問題となるものである。即ち11生燃料油が
、例えばボイラー等の燃料源として今日一般的に使用さ
れている重油よりも容に当りの単価が高く付くのでは燃
料油としての市場性がなくなり、かといって燃料油であ
る以上、燃料油を扱う1−で重要な引火点等が高いまま
では燃料油としての有効性がなくなるという問題を生じ
るものである。
In addition, when blending gasoline with this type of waste oil and reusing it as fuel oil, the +lT volume of the generated fuel oil, the dust width value, and its effectiveness as fuel oil. Coordination with the government is particularly problematic. In other words, if raw fuel oil costs more per volume than heavy oil, which is commonly used today as a fuel source for boilers, it will lose its marketability as a fuel oil; If the flash point, etc., which is important in handling fuel oil, remains high, a problem arises in that it loses its effectiveness as a fuel oil.

(発rJIの目的〕 未発IIは、使用済のこの種の植物油を、例えば重油や
灯油よりも容量当りのI′n価が安い燃料油として使用
できるよう種々改質研究を重ねた結果完成されたもので
ある。
(Purpose of Hatsura JI) Hatsuha II was completed as a result of various research into reforming this type of used vegetable oil so that it can be used as a fuel oil with a lower I'n value per volume than, for example, heavy oil or kerosene. It is what was done.

従って未発IJjの[1的は、引火点温度や発熱量等の
面で燃料油としての諸性質を満足すると共に重油等より
も容量当りの単価も安い内生燃料油を提供することにあ
る。
Therefore, the first objective of unreleased IJj is to provide endogenous fuel oil that satisfies various properties as a fuel oil in terms of flash point temperature and calorific value, and is also cheaper per volume than heavy oil etc. .

(発IJIの構L&) 未発11はこのような[1的を達成するために以下のよ
うな構成を採るものである。
(Departure IJI structure L&) In order to achieve the above goal, the non-departure 11 adopts the following structure.

即ち未発IIは、使用済の植物油100容量部に、沸点
が35℃〜250℃の鉱油25〜35容驕部を混合して
成るものである。
That is, unreleased II is made by mixing 100 parts by volume of used vegetable oil with 25 to 35 parts by volume of mineral oil having a boiling point of 35 DEG C. to 250 DEG C.

l−記使用済の植物油としては、例えば大豆油、ナタネ
油、オリーブ油、綿実油、トウモロコシ油、ヒマシ油、
ゴマ油等がある。従って例えば大豆油やナタネ油を原料
とした。いわゆる天ぷら油、サラダ油等が含まれること
は勿論である。
The used vegetable oils listed in l- include, for example, soybean oil, rapeseed oil, olive oil, cottonseed oil, corn oil, castor oil,
There is sesame oil etc. Therefore, for example, soybean oil or rapeseed oil was used as a raw material. Of course, so-called tempura oil, salad oil, etc. are included.

又1−記の鉱油としては、沸点が35℃〜180℃のガ
ソリンと、沸点が約170℃〜250℃の灯油とがある
が、本発明では燃料油としての用途や採算面を考慮して
、この内から適宜選定されるので良い。例えばガソリン
を使用して植物油を燃料油に改質する場合には、引火点
や発熱jI」の面で灯油に比べて燃料油としては好まし
いイ〆iを得ることができる。しかしながら経済上の観
点からは、容量当りの単価が安い灯油を使用する方が良
く、又灯油の引火点は約50℃位であり着火性も良好な
ことから例えばボイラーの燃料源として重油に代えて使
用する場合には灯油を使用する方が好ましい。
In addition, the mineral oil mentioned in 1- is classified into gasoline with a boiling point of 35°C to 180°C and kerosene with a boiling point of about 170°C to 250°C, but in the present invention, considering the use as fuel oil and profitability, , it is preferable to select the appropriate one from among these. For example, when gasoline is used to reform vegetable oil into fuel oil, it is possible to obtain a better fuel oil than kerosene in terms of flash point and heat generation. However, from an economic point of view, it is better to use kerosene, which has a lower unit price per capacity, and since kerosene has a flash point of about 50°C and has good ignitability, it can be used instead of heavy oil as a fuel source for boilers, for example. It is preferable to use kerosene when using it.

又使用済の植物油と、上記の鉱油との混合11合は、前
者が100容ψ部に対して後者が25〜35容ψ部であ
るが、好ましくは後者を30容;よ部とするのが良い。
In addition, when mixing 11 parts of used vegetable oil and the above-mentioned mineral oil, the former should be 100 parts by volume and the latter should be 25 to 35 parts by volume, but preferably the latter should be 30 parts by volume. is good.

鉱油の混合割合が、24合着部以下である場合には、混
合油の引火点が高くなるだけではなく1発熱量も植物油
自体の値(例えば綿実油では、約9386cal/g 
)と差異がなくなり、燃料油としては使用にイ1しなく
なる。又鉱油の混合割合が、36容iM部以上の場合に
は、鉱油の成分度合が高くなるから燃料油としては好適
であるが、反面、pf生油の容品〜当りの単価も高くな
る為、採算面で合わなくなるものである。
If the mixing ratio of mineral oil is less than 24 parts, not only will the flash point of the mixed oil be higher, but also the calorific value per unit will be higher than that of the vegetable oil itself (for example, cottonseed oil, approximately 9386 cal/g).
), and it is no longer suitable for use as fuel oil. In addition, when the mixing ratio of mineral oil is 36 parts by volume or more, it is suitable as a fuel oil because the content of mineral oil increases, but on the other hand, the unit price per container of PF raw oil also increases. , it would not be profitable from a profit standpoint.

(本発明の効果) 本発明の再生燃料油では、その引火点が、植物油の引火
点(例えばナタネ油では240℃、綿実油では約272
℃、オリーブ油では約225℃、r油脂化学便覧、1F
1本油化学協会編)よりもはるかに低く、灯油の引火点
(約50℃)より僅かに高い値を得ることができた。又
発熱量に関しても未発IJ+の再生燃料油では、植物油
(例えば綿実油では9386cal/g 、オリーブ油
では9451cal/g、 r油脂化学便覧1日本油化
学協会!&i)よりも高いイ1に改質処理されたもので
ある。しかもこの場合容に当りの単価に関しては、例え
ば重油よりも格段に安くhっだから、未発]JJの再生
燃料油を使用すれば、例えばボイラーにおける重油の代
科燃料として充分実用に耐えられる燃料になり、その結
果、重油のみによる場合より経費が大幅に節減できると
いう優れた効果を奏するものである。又未発IIでは、
使用済の植物油を燃料源として再生活用が図れることか
ら、従来のように環境汚染や廃棄用に凝固剤を用意する
等の煩わしさをも解消できるものである。
(Effects of the present invention) The recycled fuel oil of the present invention has a flash point that is higher than the flash point of vegetable oils (for example, 240°C for rapeseed oil and approximately 272°C for cottonseed oil).
°C, about 225 °C for olive oil, r Oil and Fat Chemistry Handbook, 1F
We were able to obtain a value that is much lower than that of the Japanese Oil Chemistry Association (ed.) and slightly higher than the flash point of kerosene (approximately 50°C). In addition, in terms of calorific value, unreleased IJ+ recycled fuel oil is modified to a higher value than vegetable oils (for example, 9386 cal/g for cottonseed oil, 9451 cal/g for olive oil, etc.). It is what was done. Moreover, in this case, the unit price per volume is much cheaper than, for example, heavy oil, so if JJ's recycled fuel oil is used, it can be used as a fuel that can be used as a substitute fuel for heavy oil in boilers, for example. As a result, the cost can be significantly reduced compared to using only heavy oil, which is an excellent effect. Also, in Unreleased II,
Since used vegetable oil can be recycled as a fuel source, it is possible to eliminate environmental pollution and the hassle of preparing a coagulant for disposal as in the past.

(実施例) 以下、実施例を示す。尚、実施例中、部は容j、1一部
である。
(Example) Examples are shown below. In the Examples, part means volume j and 1 part.

実施例1 大豆油とナタネ油が混入された使用済の植物油100部
に、灯油30部を加え1 ミキサーにて5〜10分間、
室温下で攪拌し混合した。
Example 1 Add 30 parts of kerosene to 100 parts of used vegetable oil mixed with soybean oil and rapeseed oil and mix in a mixer for 5 to 10 minutes.
The mixture was stirred and mixed at room temperature.

この混合油の諸性性を測定した結果、次の値を得た。As a result of measuring the various properties of this mixed oil, the following values were obtained.

この混合油を、ボイラーの燃料源として使用したが、重
油を使用したこれまでのボイラーと遜色のない熱量を得
ることができ、又引火点は、−1−記した灯油の引火点
的50℃より約12℃高いが、火はつき易かった。又混
合油の1リツトルhりの単価は、約20円でLす、容7
i1−当りのCi価も重油より安かった。
This mixed oil was used as a fuel source for a boiler, and it was able to obtain heat comparable to conventional boilers that used heavy oil, and its flash point was 50°C, which is the same as the flash point of kerosene as described in -1- Although it was about 12 degrees Celsius higher than the actual temperature, it was easy to catch fire. Also, the unit price for 1 liter of mixed oil is about 20 yen, volume 7.
The Ci value per i1- was also lower than that of heavy oil.

尚重油ノ熱醐は、約10 、000cal/gである。The weight of heavy oil is about 10,000 cal/g.

実施例2 実施例1で得られた混合油に、界面活性剤(商品名、ペ
トロフレームS−100)を3部混入し、ミキサーにて
約5分間、室温下で攪拌した。
Example 2 Three parts of a surfactant (trade name, Petroflame S-100) were mixed into the mixed oil obtained in Example 1, and the mixture was stirred for about 5 minutes at room temperature using a mixer.

得られた混合油をボイラーの燃料源とした。The resulting mixed oil was used as a fuel source for the boiler.

この場合には、界面活性剤により混合油の粘性が低下し
流動性が良くなった。又この混合油ではS02が減少し
、煤煙の発生も抑制された。その他の諸性質は、実施例
1のイ1と同様であり、ボイラーの燃料源として重油に
代えて使用することが充分「1[能であった。
In this case, the surfactant reduced the viscosity of the mixed oil and improved its fluidity. In addition, this mixed oil reduced S02 and suppressed soot generation. The other properties were the same as those in Example 1 (1), and it was sufficiently capable of being used as a boiler fuel source in place of heavy oil.

実施例3 実施例1の植物油100部に、灯油25部を加え、ミキ
サーにて5〜10分間、室温下で攪拌し混合した。この
混合油の引火点及び発a量を実施例1と同様の方法で測
定した処、引火点は約65℃、発熱Ji(は約9620
cal/g テあった。
Example 3 25 parts of kerosene was added to 100 parts of the vegetable oil of Example 1, and the mixture was stirred and mixed using a mixer at room temperature for 5 to 10 minutes. The flash point and amount of emitted a from this mixed oil were measured using the same method as in Example 1.
cal/g There was.

この混合油をボイラーの燃料源として使用した処、着火
まで数秒かかったが、火が付いた後は良く燃焼した。尚
この混合油の1リツトルちりの単価は、約18円で上っ
た。
When this mixed oil was used as a fuel source for a boiler, it took several seconds to ignite, but once it was ignited it burned well. The unit price for 1 liter of this mixed oil was approximately 18 yen.

実施例4 実施例1の植物油100部に、灯油35部を加え、ミキ
サーにて5〜lO分間、室温丁で攪拌し混合した。この
混合油をボイラーに供給した処、着火が著しく良かった
。又1−例と同様の方D:で測定した処、この混合油の
引火点は約59℃、発熱j−は約9900 cal/g
であった。尚この混合油の1リットル当りのr1価は、
約22円であった。
Example 4 35 parts of kerosene was added to 100 parts of the vegetable oil of Example 1, and the mixture was stirred and mixed in a mixer for 5 to 10 minutes at room temperature. When this mixed oil was supplied to the boiler, ignition was significantly better. Also, as measured in the same method as in Example 1-D:, the flash point of this mixed oil was approximately 59°C, and the exotherm j- was approximately 9900 cal/g.
Met. The r1 value per liter of this mixed oil is
It was about 22 yen.

Claims (1)

【特許請求の範囲】[Claims] 使用済の植物油100容量部に、沸点が35℃〜250
℃の鉱油25〜35容量部を混合して成ることを特徴と
する再生燃料油。
100 parts by volume of used vegetable oil has a boiling point of 35°C to 250°C.
A recycled fuel oil characterized in that it is formed by mixing 25 to 35 parts by volume of mineral oil at ℃.
JP15206086A 1986-06-28 1986-06-28 Regenerated fuel oil Pending JPS638483A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP15206086A JPS638483A (en) 1986-06-28 1986-06-28 Regenerated fuel oil

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP15206086A JPS638483A (en) 1986-06-28 1986-06-28 Regenerated fuel oil

Publications (1)

Publication Number Publication Date
JPS638483A true JPS638483A (en) 1988-01-14

Family

ID=15532177

Family Applications (1)

Application Number Title Priority Date Filing Date
JP15206086A Pending JPS638483A (en) 1986-06-28 1986-06-28 Regenerated fuel oil

Country Status (1)

Country Link
JP (1) JPS638483A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009544809A (en) * 2006-07-26 2009-12-17 オルターネイティヴ フュエルズ グループ インコーポレイテッド Alternative organic fuel formulations containing vegetable oil

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009544809A (en) * 2006-07-26 2009-12-17 オルターネイティヴ フュエルズ グループ インコーポレイテッド Alternative organic fuel formulations containing vegetable oil

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