JPH01185394A - Emulsifier for heavy oil/water mixed fuel - Google Patents
Emulsifier for heavy oil/water mixed fuelInfo
- Publication number
- JPH01185394A JPH01185394A JP852888A JP852888A JPH01185394A JP H01185394 A JPH01185394 A JP H01185394A JP 852888 A JP852888 A JP 852888A JP 852888 A JP852888 A JP 852888A JP H01185394 A JPH01185394 A JP H01185394A
- Authority
- JP
- Japan
- Prior art keywords
- emulsifier
- heavy oil
- oxide
- emulsion
- active hydrogen
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- 239000003995 emulsifying agent Substances 0.000 title claims abstract description 22
- 239000000295 fuel oil Substances 0.000 title claims abstract description 22
- 239000000446 fuel Substances 0.000 title claims abstract description 19
- XLYOFNOQVPJJNP-ZSJDYOACSA-N heavy water Substances [2H]O[2H] XLYOFNOQVPJJNP-ZSJDYOACSA-N 0.000 title claims description 8
- 125000002947 alkylene group Chemical group 0.000 claims abstract description 11
- IAYPIBMASNFSPL-UHFFFAOYSA-N Ethylene oxide Chemical compound C1CO1 IAYPIBMASNFSPL-UHFFFAOYSA-N 0.000 claims abstract description 10
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims abstract description 8
- 229910052739 hydrogen Inorganic materials 0.000 claims abstract description 8
- 239000001257 hydrogen Substances 0.000 claims abstract description 8
- 239000004721 Polyphenylene oxide Substances 0.000 claims abstract description 7
- 229920000570 polyether Polymers 0.000 claims abstract description 7
- 239000007795 chemical reaction product Substances 0.000 claims abstract description 3
- 150000001875 compounds Chemical class 0.000 claims description 11
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 8
- 125000003118 aryl group Chemical group 0.000 claims description 6
- 239000000839 emulsion Substances 0.000 abstract description 20
- WVDDGKGOMKODPV-UHFFFAOYSA-N Benzyl alcohol Chemical compound OCC1=CC=CC=C1 WVDDGKGOMKODPV-UHFFFAOYSA-N 0.000 abstract description 6
- -1 phenol) Chemical class 0.000 abstract description 5
- YCIMNLLNPGFGHC-UHFFFAOYSA-N catechol Chemical compound OC1=CC=CC=C1O YCIMNLLNPGFGHC-UHFFFAOYSA-N 0.000 abstract description 4
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N Phenol Chemical compound OC1=CC=CC=C1 ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 abstract description 2
- GOOHAUXETOMSMM-UHFFFAOYSA-N Propylene oxide Chemical compound CC1CO1 GOOHAUXETOMSMM-UHFFFAOYSA-N 0.000 abstract description 2
- WYURNTSHIVDZCO-UHFFFAOYSA-N Tetrahydrofuran Chemical compound C1CCOC1 WYURNTSHIVDZCO-UHFFFAOYSA-N 0.000 abstract description 2
- 150000001298 alcohols Chemical class 0.000 abstract description 2
- 235000019445 benzyl alcohol Nutrition 0.000 abstract description 2
- 150000002989 phenols Chemical class 0.000 abstract description 2
- 150000005846 sugar alcohols Polymers 0.000 abstract description 2
- 230000002035 prolonged effect Effects 0.000 abstract 1
- 239000003921 oil Substances 0.000 description 6
- 239000010426 asphalt Substances 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 238000003756 stirring Methods 0.000 description 3
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 2
- 235000014113 dietary fatty acids Nutrition 0.000 description 2
- 229930195729 fatty acid Natural products 0.000 description 2
- 239000000194 fatty acid Substances 0.000 description 2
- 230000007774 longterm Effects 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- WQGWDDDVZFFDIG-UHFFFAOYSA-N pyrogallol Chemical compound OC1=CC=CC(O)=C1O WQGWDDDVZFFDIG-UHFFFAOYSA-N 0.000 description 2
- GHMLBKRAJCXXBS-UHFFFAOYSA-N resorcinol Chemical compound OC1=CC=CC(O)=C1 GHMLBKRAJCXXBS-UHFFFAOYSA-N 0.000 description 2
- 230000003068 static effect Effects 0.000 description 2
- KJCVRFUGPWSIIH-UHFFFAOYSA-N 1-naphthol Chemical compound C1=CC=C2C(O)=CC=CC2=C1 KJCVRFUGPWSIIH-UHFFFAOYSA-N 0.000 description 1
- JKTAIYGNOFSMCE-UHFFFAOYSA-N 2,3-di(nonyl)phenol Chemical compound CCCCCCCCCC1=CC=CC(O)=C1CCCCCCCCC JKTAIYGNOFSMCE-UHFFFAOYSA-N 0.000 description 1
- VURUNMWLBDYAMB-UHFFFAOYSA-N 2-butylnaphthalen-1-ol Chemical compound C1=CC=CC2=C(O)C(CCCC)=CC=C21 VURUNMWLBDYAMB-UHFFFAOYSA-N 0.000 description 1
- CYEJMVLDXAUOPN-UHFFFAOYSA-N 2-dodecylphenol Chemical compound CCCCCCCCCCCCC1=CC=CC=C1O CYEJMVLDXAUOPN-UHFFFAOYSA-N 0.000 description 1
- SRJCJJKWVSSELL-UHFFFAOYSA-N 2-methylnaphthalen-1-ol Chemical compound C1=CC=CC2=C(O)C(C)=CC=C21 SRJCJJKWVSSELL-UHFFFAOYSA-N 0.000 description 1
- QTWJRLJHJPIABL-UHFFFAOYSA-N 2-methylphenol;3-methylphenol;4-methylphenol Chemical compound CC1=CC=C(O)C=C1.CC1=CC=CC(O)=C1.CC1=CC=CC=C1O QTWJRLJHJPIABL-UHFFFAOYSA-N 0.000 description 1
- WJQOZHYUIDYNHM-UHFFFAOYSA-N 2-tert-Butylphenol Chemical compound CC(C)(C)C1=CC=CC=C1O WJQOZHYUIDYNHM-UHFFFAOYSA-N 0.000 description 1
- 229930185605 Bisphenol Natural products 0.000 description 1
- IGFHQQFPSIBGKE-UHFFFAOYSA-N Nonylphenol Natural products CCCCCCCCCC1=CC=C(O)C=C1 IGFHQQFPSIBGKE-UHFFFAOYSA-N 0.000 description 1
- 239000004698 Polyethylene Substances 0.000 description 1
- 238000000889 atomisation Methods 0.000 description 1
- IISBACLAFKSPIT-UHFFFAOYSA-N bisphenol A Chemical compound C=1C=C(O)C=CC=1C(C)(C)C1=CC=C(O)C=C1 IISBACLAFKSPIT-UHFFFAOYSA-N 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 229920001577 copolymer Polymers 0.000 description 1
- 229930003836 cresol Natural products 0.000 description 1
- 239000010779 crude oil Substances 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000004945 emulsification Methods 0.000 description 1
- 230000001804 emulsifying effect Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000011156 evaluation Methods 0.000 description 1
- 239000002803 fossil fuel Substances 0.000 description 1
- 238000009775 high-speed stirring Methods 0.000 description 1
- 239000003949 liquefied natural gas Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- SNQQPOLDUKLAAF-UHFFFAOYSA-N nonylphenol Chemical compound CCCCCCCCCC1=CC=CC=C1O SNQQPOLDUKLAAF-UHFFFAOYSA-N 0.000 description 1
- QBDSZLJBMIMQRS-UHFFFAOYSA-N p-Cumylphenol Chemical compound C=1C=C(O)C=CC=1C(C)(C)C1=CC=CC=C1 QBDSZLJBMIMQRS-UHFFFAOYSA-N 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 238000005504 petroleum refining Methods 0.000 description 1
- 229920000573 polyethylene Polymers 0.000 description 1
- 238000006116 polymerization reaction Methods 0.000 description 1
- 230000000379 polymerizing effect Effects 0.000 description 1
- 229940079877 pyrogallol Drugs 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000004094 surface-active agent Substances 0.000 description 1
- 150000003739 xylenols Chemical class 0.000 description 1
Landscapes
- Liquid Carbonaceous Fuels (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は重質油を水に分散乳化させて水中油滴型の重質
油、水混合燃料を製造するための重質油、水混合燃料用
乳化剤に関する。本発明の乳化剤を用いて得られる該混
合燃料は、液体燃料を使用する原拗機・関連製品一般に
おいて用いられるが、特にボイラ、ディーゼル機関等に
用いて効果が犬である。[Detailed Description of the Invention] [Industrial Application Field] The present invention is a method for dispersing and emulsifying heavy oil in water to produce oil-in-water type heavy oil and water-mixed fuel. This invention relates to emulsifiers for fuel. The mixed fuel obtained using the emulsifier of the present invention is used in general for industrial machinery and related products that use liquid fuel, but is especially effective when used in boilers, diesel engines, etc.
原油、石炭及びLNGに含まれない化石燃料資源であっ
て、その埋蔵量の大きな点から現在注目されているもの
に、オイルサンドや天然アスファルト等の重質油がある
。これ等の重質油は、通常減圧蒸留残分である420℃
〜450℃以上の重質留分を約60〜70%以上含有す
る、重質な油状物質であり、そのままでは数万センチポ
アズ以上の高粘性である。そのために燃料として使用す
るには、ハンドリング、噴霧による霧化等において使い
にくいものである。Fossil fuel resources not included in crude oil, coal, and LNG that are currently attracting attention because of their large reserves include heavy oils such as oil sands and natural asphalt. These heavy oils are usually distilled under reduced pressure at 420°C.
It is a heavy oily substance containing approximately 60 to 70% or more of heavy fractions of ~450°C or higher, and has a high viscosity of tens of thousands of centipoise or higher as it is. Therefore, when used as a fuel, it is difficult to handle, atomize by spraying, etc.
これ等の重質油を水と混合して水中油滴形(0/W型)
のエマルジョンとすれば、媒体の水に近い低粘度化を達
成できて上記の困難が解消できるわけであるが、一方で
この低粘度化によって重質油含有量が下がることは、燃
料として好壕しくない。These heavy oils are mixed with water to form oil droplets in water (0/W type).
If it is an emulsion, it is possible to achieve a low viscosity similar to that of water as a medium and overcome the above difficulties, but on the other hand, this lower viscosity lowers the heavy oil content, which makes it less suitable as a fuel. It's not right.
であシ、従来このような乳化剤として脂肪酸エステル系
や高級アルコール系の界面活性剤が用いられている。Conventionally, fatty acid ester-based or higher alcohol-based surfactants have been used as such emulsifiers.
しかしながら、脂肪酸エステル系や高級アルコール系の
乳化剤は、重質油乳化の性能が不足していた。例えばこ
れ等の乳化剤を用いた重質油のエマルジョン燃料を外国
から輸入すると、輸送の途中で重質油の粒子同志の会合
による粗粒化をさたし、国内到着時点ではすでに燃料と
しては好ましくない状態になっていることが多い。However, fatty acid ester-based and higher alcohol-based emulsifiers lack heavy oil emulsification performance. For example, if heavy oil emulsion fuel using these emulsifiers is imported from a foreign country, it will become coarse due to the association of heavy oil particles during transportation, and by the time it arrives in Japan, it is already undesirable as a fuel. It is often absent.
本発明はこのような現状に鑑みてなされたものであって
、重質油を0/W ffiに分散させてその油分濃度が
70〜78重量%の高濃度で、しかも長期間安定性を保
ち得るエマルジョン燃料として調整するに適した乳化剤
の提供を目的とするものである。The present invention has been made in view of the current situation, and is a method of dispersing heavy oil in 0/W ffi to have a high oil concentration of 70 to 78% by weight and maintaining stability for a long period of time. The object of the present invention is to provide an emulsifier suitable for preparing an emulsion fuel.
本発明は分子内に芳香族環及び活性水素を有する化合物
とエチレンオキシドを必須成分として含むアルキレンオ
キシドとの反応生成物であるポリエーテル化合物を主成
分とする水中油滴型の重質油、水混合燃料用乳化剤であ
る。The present invention is an oil-in-water type heavy oil, which is a water-mixed oil droplet type heavy oil whose main component is a polyether compound which is a reaction product of a compound having an aromatic ring and active hydrogen in the molecule and an alkylene oxide containing ethylene oxide as an essential component. It is an emulsifier for fuel.
本発明の乳化剤の主成分たるポリエーテル化合物として
は、分子内に芳香族環及び活性水素を有する化合物と、
エチレンオキシドを必須成分として含むアルキレンオキ
シドが重合して得られた共重合体が用いられる。分子内
に芳香族環及び活性水素を有する化合物とエチレンオキ
シドの重合反応は次式のように進行する。The polyether compound which is the main component of the emulsifier of the present invention includes a compound having an aromatic ring and an active hydrogen in the molecule;
A copolymer obtained by polymerizing alkylene oxide containing ethylene oxide as an essential component is used. The polymerization reaction between a compound having an aromatic ring and active hydrogen in the molecule and ethylene oxide proceeds as shown in the following formula.
ここで、本発明における分子内に芳香族環及び活性水素
を有する化合物の具体例としては、以下のものが挙げら
れる。Here, specific examples of compounds having an aromatic ring and active hydrogen in the molecule in the present invention include the following.
■ フェノール、クレゾール、ターシャリ−ブチルフェ
ノール、オクチルフェノール、ノニルフェノール、ジノ
ニルフェノール、ドデシルフェノール、キシレノール、
ナフトール、メチルナフトール、ブチルナフトール、パ
ラクミルフェノール等のフェノール類。■ Phenol, cresol, tert-butylphenol, octylphenol, nonylphenol, dinonylphenol, dodecylphenol, xylenol,
Phenols such as naphthol, methylnaphthol, butylnaphthol, paracumylphenol.
■ ベンジルアルコールなどの1価アルコール類。■ Monohydric alcohols such as benzyl alcohol.
■ カテコール、レゾルシン、ピロガロール、ビスフェ
ノールA1 フェノールホルマリン縮合物などの多価ア
ルコール。■ Polyhydric alcohols such as catechol, resorcinol, pyrogallol, bisphenol A1, and phenol-formalin condensates.
これら分子内に芳香族環および活性水素を有する化合物
に付加されるアルキレンオキシドとしては、エチレンオ
キシドが単独で、又は他のアルキレンオキシドとともに
用いられる。As the alkylene oxide added to these compounds having an aromatic ring and active hydrogen in the molecule, ethylene oxide is used alone or together with other alkylene oxides.
全アルキレンオキシド中のエチレンオキシドの割合は、
80〜100重量%が適当である。The proportion of ethylene oxide in the total alkylene oxide is
80 to 100% by weight is suitable.
エチレンオキシド以外のアルキレンオキシドとしては例
えばプロピレンオキシド、ブチレンオキシドなどが用い
られる。Examples of alkylene oxides other than ethylene oxide include propylene oxide and butylene oxide.
本発明に係わるポリエーテル化合物は重量平均分子量で
400〜200oが好適であり、好ましくは500〜2
000である。The weight average molecular weight of the polyether compound according to the present invention is preferably 400 to 200°, preferably 500 to 200°.
It is 000.
本発明の乳化剤は、0/wエマルジョン中に0.05〜
2重量%、好ましくは0.1〜1重量%の範囲で含まれ
るように象加するのが適当である。本発明の乳化剤を用
いて混合燃料を得る原料とする重質、高粘性油としては
天然アスファルト、アサバスカビチューメン等の他、石
油精製の釜残であるアスファルトを多量に含んだ油類を
使用することができる。The emulsifier of the present invention can be used in a 0/w emulsion from 0.05 to
It is appropriate to add it in an amount of 2% by weight, preferably in the range of 0.1 to 1% by weight. As the heavy, highly viscous oil used as the raw material for obtaining the mixed fuel using the emulsifier of the present invention, oils containing a large amount of asphalt, which is the residue of petroleum refining, may be used in addition to natural asphalt, athabasca tumene, etc. Can be done.
本発明の乳化剤を用いて重質油、水混合燃料油エマルジ
ョンを製造する具体的方法は、重質油と水とをそれぞれ
の所定量比に、−船釣には、重質油を70〜78重量え
になるように配合し、これに本発明の乳化剤を所定量刃
口えて攪拌することで重質油を微粒の液滴粒になるよう
にして調整する。攪拌手段としてはごく一般的なパドル
形、ヘリカルリボン形の攪拌でもよいが、好ましくはラ
インミキサー等として知られている高速攪拌を行なうの
がよい。またこれら両方の攪拌手段を併用してもよい結
果を得ることができる。A specific method for producing a mixed fuel oil emulsion of heavy oil and water using the emulsifier of the present invention is to mix heavy oil and water at respective predetermined ratios; A predetermined amount of the emulsifier of the present invention is added to the mixture and stirred to form heavy oil into fine droplets. The stirring means may be a very common paddle-type or helical ribbon-type stirring, but it is preferable to use a high-speed stirring known as a line mixer or the like. Further, good results can be obtained by using both of these stirring means in combination.
本発明の乳化剤を用いることで重質油/水エマルジヨン
燃料を低粘度化し且つ長期間の貯蔵でも従来のものよシ
そのエマルジョン燃料定に保つことができる。By using the emulsifier of the present invention, the viscosity of heavy oil/water emulsion fuel can be lowered and the emulsion fuel can be kept more constant than conventional emulsion fuels even during long-term storage.
次のその一実施例について説明する。An example of this will be described below.
〔実施例〕
表1に示す本発明の乳化剤を用いて、表2に示すように
重質油、水、乳化剤を配合し、混合して全量を500.
9とした後、ダブルヘリカルリボン翼の攪拌機を用いて
回転数6 Orpmで5分間混合した後、ホモミキサー
(商品名:特殊機化工(株)製)にて4000 rpm
で5分間混合してエマルジョンを調整シタ。[Example] Using the emulsifier of the present invention shown in Table 1, heavy oil, water, and emulsifier were blended as shown in Table 2, and mixed to bring the total amount to 500.
9, and then mixed for 5 minutes at a rotation speed of 6 orpm using a stirrer with double helical ribbon blades, and then mixed at 4000 rpm using a homo mixer (product name: manufactured by Tokushu Kikako Co., Ltd.).
Adjust the emulsion by mixing for 5 minutes.
このエマルジョンの流動性及び静置安定性を以下の方法
により評価した。評価結果を表2に1とめて示す。The fluidity and static stability of this emulsion were evaluated by the following methods. The evaluation results are summarized in Table 2.
1)流動性
調整したエマルジョンの粘度はブルックフィールド粘度
計(崖20−タ、50回転、1分後測定)で粘度を測定
すると共に、エマルションの一定量を100メツシユの
ふるいを通し、10分後に残ったふるい上の量を測定し
て得たエマルジョンのふるい上残留率〔ふるい上桟留分
/供試エマルジョン量(重量%)〕から微粒化率を求め
、以下のように評価した。1) The viscosity of the emulsion whose fluidity has been adjusted is determined by measuring the viscosity with a Brookfield viscometer (20-meter cliff, 50 revolutions, measured after 1 minute), and passing a certain amount of the emulsion through a 100-mesh sieve and measuring after 10 minutes. The atomization rate was determined from the residual rate of the emulsion on the sieve (fraction on the sieve/sample emulsion amount (weight %)) obtained by measuring the amount remaining on the sieve, and was evaluated as follows.
○ :良 好 500 cp以下 20%以下Δ
:不十分 500へ1000cp 20へ50%×
;不 良 1000cp以上 50%以上2)
静置安定性
上記のエマルジョンヲ密栓ポリ瓶に入れ、室温にて一ケ
月間株管した仮、上記1)の流動性評価を行なった。○: Good 500 cp or less 20% or less Δ
: Insufficient 1000 cp to 500 50% to 20
;Defect 1000cp or more 50% or more2)
Static Stability The above emulsion was placed in a sealed polyethylene bottle and kept at room temperature for one month to evaluate the fluidity as described in 1) above.
表 1 ポリエーテル化合物の性状(注)go:エ
チレンオキサイド
RO:その他のアルキレンオキサイド
〔発明の効果〕
本発明の重質油・水混合燃料用乳化剤は、これを用いる
ことによシ重質油/水エマルジョン燃料を低粘度化し、
且つ長期間の貯蔵でも従来のものよpそのエマルジョン
を安定に保つことができるという効果を奏する。Table 1 Properties of polyether compounds (Note) go: Ethylene oxide RO: Other alkylene oxides [Effects of the invention] By using the emulsifier for heavy oil/water mixed fuel of the present invention, By reducing the viscosity of water emulsion fuel,
In addition, even during long-term storage, the emulsion can be kept more stable than conventional emulsions.
Claims (1)
ンオキシドを必須成分として含むアルキレンオキシドと
の反応生成物であるポリエーテル化合物を主成分とする
水中油滴型の重質油、水混合燃料用乳化剤。An oil-in-water type emulsifier for heavy oil and water-mixed fuels whose main component is a polyether compound, which is a reaction product of a compound having an aromatic ring and active hydrogen in the molecule and an alkylene oxide containing ethylene oxide as an essential component. .
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63008528A JPH0832901B2 (en) | 1988-01-20 | 1988-01-20 | Heavy oil, water mixed fuel oil and method for producing the same |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63008528A JPH0832901B2 (en) | 1988-01-20 | 1988-01-20 | Heavy oil, water mixed fuel oil and method for producing the same |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH01185394A true JPH01185394A (en) | 1989-07-24 |
JPH0832901B2 JPH0832901B2 (en) | 1996-03-29 |
Family
ID=11695649
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP63008528A Expired - Lifetime JPH0832901B2 (en) | 1988-01-20 | 1988-01-20 | Heavy oil, water mixed fuel oil and method for producing the same |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0832901B2 (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5851245A (en) * | 1996-05-23 | 1998-12-22 | Kao Corporation | Method for producing superheavy oil emulsion fuel and fuel produced thereby |
US5879419A (en) * | 1995-06-01 | 1999-03-09 | Kao Corporation | Method for producing superheavy oil emulsion fuel |
KR100743826B1 (en) * | 2000-05-19 | 2007-07-30 | 다이호고교가부시키가이샤 | Fuel additive for bituminous heavy oil/water emulsion fuel and method of combustion |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5372015A (en) * | 1976-12-08 | 1978-06-27 | Toyo Tire & Rubber Co Ltd | Pre-mixer for emulsion fuel prepataiton |
US4666457A (en) * | 1984-09-24 | 1987-05-19 | Petroleum Fermentations N.V. | Method for reducing emissions utilizing pre-atomized fuels |
JPS6354498A (en) * | 1986-06-17 | 1988-03-08 | インテヴエツプ,エス.エイ | Method for producing natural liquid fuel to burn the same and natural liquid fuel formed as oil in emulsion |
-
1988
- 1988-01-20 JP JP63008528A patent/JPH0832901B2/en not_active Expired - Lifetime
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5372015A (en) * | 1976-12-08 | 1978-06-27 | Toyo Tire & Rubber Co Ltd | Pre-mixer for emulsion fuel prepataiton |
US4666457A (en) * | 1984-09-24 | 1987-05-19 | Petroleum Fermentations N.V. | Method for reducing emissions utilizing pre-atomized fuels |
US4666457B1 (en) * | 1984-09-24 | 1990-05-01 | Petroleum Fermentations | |
JPS63501578A (en) * | 1985-10-15 | 1988-06-16 | インタヴェップ,ソシエタ アノニム | Method for reducing emissions using pre-atomized fuel |
JPS6354498A (en) * | 1986-06-17 | 1988-03-08 | インテヴエツプ,エス.エイ | Method for producing natural liquid fuel to burn the same and natural liquid fuel formed as oil in emulsion |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5879419A (en) * | 1995-06-01 | 1999-03-09 | Kao Corporation | Method for producing superheavy oil emulsion fuel |
US5851245A (en) * | 1996-05-23 | 1998-12-22 | Kao Corporation | Method for producing superheavy oil emulsion fuel and fuel produced thereby |
KR100743826B1 (en) * | 2000-05-19 | 2007-07-30 | 다이호고교가부시키가이샤 | Fuel additive for bituminous heavy oil/water emulsion fuel and method of combustion |
Also Published As
Publication number | Publication date |
---|---|
JPH0832901B2 (en) | 1996-03-29 |
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