JP2007238945A - Fuel oil composition - Google Patents

Fuel oil composition Download PDF

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JP2007238945A
JP2007238945A JP2007060231A JP2007060231A JP2007238945A JP 2007238945 A JP2007238945 A JP 2007238945A JP 2007060231 A JP2007060231 A JP 2007060231A JP 2007060231 A JP2007060231 A JP 2007060231A JP 2007238945 A JP2007238945 A JP 2007238945A
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fuel oil
carbon atoms
composition
composition according
copolymer
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JP5178029B2 (en
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Masahiro Oraku
正浩 大楽
Robert Dryden Tack
ドライデン タック ロバート
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Infineum International Ltd
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    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L10/00Use of additives to fuels or fires for particular purposes
    • C10L10/14Use of additives to fuels or fires for particular purposes for improving low temperature properties
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/143Organic compounds mixtures of organic macromolecular compounds with organic non-macromolecular compounds
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/18Organic compounds containing oxygen
    • C10L1/192Macromolecular compounds
    • C10L1/195Macromolecular compounds obtained by reactions involving only carbon-to-carbon unsaturated bonds
    • C10L1/197Macromolecular compounds obtained by reactions involving only carbon-to-carbon unsaturated bonds derived from monomers containing a carbon-to-carbon unsaturated bond and an acyloxy group of a saturated carboxylic or carbonic acid
    • C10L1/1973Macromolecular compounds obtained by reactions involving only carbon-to-carbon unsaturated bonds derived from monomers containing a carbon-to-carbon unsaturated bond and an acyloxy group of a saturated carboxylic or carbonic acid mono-carboxylic
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/18Organic compounds containing oxygen
    • C10L1/192Macromolecular compounds
    • C10L1/198Macromolecular compounds obtained otherwise than by reactions involving only carbon-to-carbon unsaturated bonds homo- or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon to carbon double bond, and at least one being terminated by an acyloxy radical of a saturated carboxylic acid, of carbonic acid
    • C10L1/1981Condensation polymers of aldehydes or ketones
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/22Organic compounds containing nitrogen
    • C10L1/222Organic compounds containing nitrogen containing at least one carbon-to-nitrogen single bond
    • C10L1/2222(cyclo)aliphatic amines; polyamines (no macromolecular substituent 30C); quaternair ammonium compounds; carbamates
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/22Organic compounds containing nitrogen
    • C10L1/222Organic compounds containing nitrogen containing at least one carbon-to-nitrogen single bond
    • C10L1/224Amides; Imides carboxylic acid amides, imides

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  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Engineering & Computer Science (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Liquid Carbonaceous Fuels (AREA)

Abstract

<P>PROBLEM TO BE SOLVED: To provide a fuel oil composition having improved characteristics. <P>SOLUTION: The fuel oil composition contains an intermediate fraction fuel having >0.1 mass% residual carbon, and one or more ethylene-vinyl ester copolymers and one or more phenol resins having 400-10,000 g/mol molecular weight as additives. <P>COPYRIGHT: (C)2007,JPO&INPIT

Description

本発明は、燃料油組成物に関するものである。   The present invention relates to a fuel oil composition.

(発明の背景)
いくつかの中間留出燃料油は、通常よりも高い残留炭素レベルによって特徴付けられる。そのような高残留炭素レベルは、残留燃料油を中間留出燃料油に添加することにより生じ、中間留出燃料油を変性させるために行われ、それを「路上」自動車用の燃料として望ましくないものにする。そのような変性燃料油の例としては、重油Aとも呼ばれ、日本で見られる燃料油である。
重油Aは、暖房用オイルとして使用され、したがって使用するとき、徐冷条件を経て、バーナーに供給される前にメッシュフィルターを通過できることが必要である。エチレン-酢酸ビニルコポリマーのような中間流出低温流動性添加剤の使用によって、重油Aが徐冷条件を満たすのを補助することが知られている。
しかしながら、特開平10-274616号公報に記載されるように、暖房用オイルとしての重油Aの上記使用をシミュレートする試験が紹介されている。エチレン-ビニルエステルコポリマー添加剤を用いて、この試験で必要な性能を達成すること(すなわち、低い目的の温度で「合格」すること)が困難であることがわかった。
(Background of the Invention)
Some middle distillate fuel oils are characterized by higher residual carbon levels than normal. Such high residual carbon levels are created by adding residual fuel oil to middle distillate fuel oil, which is done to denature middle distillate fuel oil, making it undesirable as a fuel for "on the road" automobiles Make things. An example of such a modified fuel oil is also called heavy oil A and is a fuel oil found in Japan.
Heavy oil A is used as a heating oil, and therefore when used, it needs to be able to pass through a mesh filter before being supplied to the burner via slow cooling conditions. It is known to assist heavy oil A in satisfying the slow cooling condition through the use of intermediate effluent cold flow additives such as ethylene-vinyl acetate copolymers.
However, as described in JP-A-10-274616, a test for simulating the above-described use of heavy oil A as a heating oil is introduced. Using ethylene-vinyl ester copolymer additives, it has been found difficult to achieve the required performance in this test (ie, “pass” at low target temperatures).

(発明の要約)
驚いたことに、本明細書のデータによって示されるように、上述の試験において重油A及び同様の油における改善された特性が、ワックス結晶改良剤ではない1つ以上のポリマー、すなわち1つ以上のエチレン-ビニルエステルコポリマーと組合せた低分子量フェノール樹脂を使用することによって達成できることを見出した。
このように、第1の局面では、本発明は、(A)0.1質量%よりも多い残留炭素(ASTM D189による測定)を有する過半量の中間留分燃料油;及び少割合の以下の各添加剤を含む燃料油組成物を提供する:(B)1つ以上の、エチレン及び1〜18個の炭素原子を含むアルキル基を有するビニルエステルのコポリマー;及び(C)1つ以上の、分子量が400〜10,000g/モルであるフェノール樹脂。
本明細書において、以下の用語及び表現は、使用される場合、以下に記載された意味を有するものとする:
「活性成分」又は「(a.i.)」は希釈剤又は溶媒ではない添加材料を意味する。
「含む」又は同種の用語は、定められた特徴、工程、又は完全体(integers)又は成分が存在することを示すが、1又は2以上の他の特徴、工程、完全体、成分又はこれらのグループの存在又は追加を排除しない。
「からなる」又は「から本質的になる」と言う表現又は同種の用語は、「含む」又は同種の用語に含まれる場合があり、この場合、「から本質的になる」は、それが適用される組成物の特徴に実質的に影響を及ぼさない物質を含めることを認める。
「過半量」とは、組成物の50質量%を越えることを意味する。
「少割合」とは、組成物の50質量%未満を意味する。
また、当然のことながら、使用される、必須及び任意の、及び通常の種々の成分は、配合、保管又は使用の条件下で反応し得、また本発明は、任意のそのような反応の結果として得ることができる、又は得た生成物を与える。
さらに、当然のことながら、本明細書に記載される任意の上限及び下限の量、範囲及び比の限定は、独立して組み合わせてもよい。
(Summary of the Invention)
Surprisingly, as shown by the data herein, the improved properties in heavy oil A and similar oils in the above test indicate that one or more polymers that are not wax crystal modifiers, ie one or more It has been found that this can be achieved by using a low molecular weight phenolic resin in combination with an ethylene-vinyl ester copolymer.
Thus, in a first aspect, the present invention provides (A) a majority amount of middle distillate fuel oil having greater than 0.1% by weight residual carbon (as measured by ASTM D189); and a small proportion of each of the following additions: A fuel oil composition comprising an agent is provided: (B) a copolymer of one or more vinyl esters having ethylene and an alkyl group containing 1 to 18 carbon atoms; and (C) one or more molecular weights. Phenolic resin that is 400-10,000 g / mol.
As used herein, the following terms and expressions, when used, shall have the meanings set forth below:
“Active ingredient” or “(ai)” means an additive material that is not a diluent or solvent.
“Contains” or like terms indicate that a defined feature, process, or integers or component is present, but one or more other features, processes, integrals, components, or these Does not exclude the presence or addition of groups.
The expression “consisting of” or “consisting essentially of” or similar terms may be included in the term “comprising” or similar terms, in which case “consisting essentially of” It is permissible to include substances that do not substantially affect the characteristics of the composition.
“Major amount” means greater than 50% by weight of the composition.
“Minor proportion” means less than 50% by weight of the composition.
Also, it will be appreciated that the essential and optional and usual components used may react under the conditions of formulation, storage or use, and the present invention may be the result of any such reaction. To give or give the product obtained.
Furthermore, it should be understood that any upper and lower amount, range and ratio limitations set forth herein may be independently combined.

(発明の詳細な説明)
適切な場合には、本発明の各及びすべての局面に関連する本発明の特徴は、より詳細に以下のとおりに記載される。
(Detailed description of the invention)
Where appropriate, the features of the invention relating to each and every aspect of the invention are described in more detail as follows.

(中間留出燃料油(A))
中間留出燃料油は、一般に110℃〜500℃、例えば150℃〜400℃又は170℃〜370℃の範囲内で沸騰する(ASTM D86に従う)石油系燃料油である。この燃料油は、常圧留出物又は減圧留出物、又は直留及び熱及び/又は接触分解又は水素化分解留出物の任意比率のブレンドを含んでもよい。好適には、本発明では、この燃料油は広範囲に沸騰し、高い終点を有し、中程度のワックス含有量(例えば、その曇り点よりも10℃低い温度で約3質量%)を有する。
記載したように、中間流出燃料油は0.1質量%よりも多い残留炭素を有する。これは、蒸留底(distillation bottoms)のサンプル(10g)を、風袋を測定した坩堝にいれ、分解蒸留に供して指定期間の激しい加熱の際に熱分解及びコーキング反応を生じさせる、コンラドソン法(ASTM D189)によって測定される。冷却及び重さを再度測定して残っている量を計算した後、結果を、10%蒸留残滓におけるコンラドソン残留炭素(%)として報告する。
残留炭素は、0.1〜4質量%の範囲であってもよく、例えば0.2〜2質量%の範囲であり、好ましくは0.2〜1質量%の範囲である。さらに好ましくは、残留炭素は、0.2〜0.5質量%の範囲である。
上述の炭素値は、中間留出燃料油と残留燃料油(しばしば、残留物(residuum)又は残油(resid)と呼ばれる)との混合によって達成してもよい。残燃料油は、蒸留(常圧であってもよく、常圧に続く減圧蒸留であってもよい)から得られる原油の不揮発性部分である。
典型的には、中間留出燃料油は、2〜10質量%、例えば5〜10質量%の残燃料油を含んでもよい。
(Middle distillate fuel oil (A))
Middle distillate fuel oils are petroleum-based fuel oils that generally boil (according to ASTM D86) in the range of 110 ° C to 500 ° C, such as 150 ° C to 400 ° C or 170 ° C to 370 ° C. The fuel oil may comprise a blend of atmospheric distillate or vacuum distillate, or any ratio of straight and heat and / or catalytic cracking or hydrocracking distillate. Preferably, in the present invention, the fuel oil boils over a wide range, has a high endpoint, and has a moderate wax content (eg, about 3% by weight at a temperature 10 ° C. below its cloud point).
As noted, the intermediate spill fuel oil has more than 0.1 mass% residual carbon. This is done by placing a sample (10 g) of distillation bottoms into a tared crucible and subjecting it to cracking distillation to cause pyrolysis and coking reactions during intense heating for a specified period. D189). After re-cooling and weighing and calculating the amount remaining, the results are reported as% Conradson carbon in 10% distillation residue.
The residual carbon may be in the range of 0.1 to 4% by mass, for example in the range of 0.2 to 2% by mass, and preferably in the range of 0.2 to 1% by mass. More preferably, the residual carbon is in the range of 0.2 to 0.5% by mass.
The carbon values described above may be achieved by mixing middle distillate fuel oil and residual fuel oil (often referred to as residue or residue). Residual fuel oil is the non-volatile portion of crude oil obtained from distillation (which may be normal pressure or may be vacuum distillation following normal pressure).
Typically, the middle distillate fuel oil may comprise 2-10% by weight residual fuel oil, for example 5-10% by weight.

(添加剤(B))
添加剤(B)では、ビニルエステルは、好ましくは式CH2=CR1OOCR2(I)(式中、R1は水素原子又はメチル基を表し、R2は1〜4個の炭素原子を有するアルキル基を表す。)を有する。より好ましくは、ビニルエステルは酢酸ビニルである。
コポリマーはターポリマーを含み、このターポリマーは、エチレン、前記ビニルエステル及び5〜15個の炭素原子を含むアルキル基を有する第2の異なるビニルエステルのターポリマーである。第2ビニルエステルは、使用する場合、好ましくはCH2=CR3OOCR4(II)(式中、R3は水素原子又はメチル基を表し、R4は5個以上、例えば5〜15個の炭素原子を有するアルキル基を表し、好ましくは7〜15個の炭素原子を有する分枝鎖アルキル基である。)を有する。例として、第2ビニルエステルは、ビニル2-エチルヘキサノアート、ビニルネオデカノアート又はビニルオクタノアートであってもよい。
本明細書で使用する「ターポリマー」という用語は、ポリマーが少なくとも3つの異なる繰り返し単位を有すること、すなわち少なくとも3つの異なるモノマー、すなわちエチレン、モノマー(I)及びモノマー(II)から誘導されることを要求する。前記用語は、4つ以上のモノマーから誘導できるポリマーを含み、例えばポリマーは2つ以上のモノマー(I)及び(II)から誘導できる単位を含んでもよく、及び/又は式CH2=CR1OOCR5(III)(式中、R5は5個以上の炭素原子を有する、R4によって定義されるもの以外のヒドロカルビル基を表す。)のモノマーから誘導できる単位を含んでもよい。
このように、本発明の方法は、2つ以上のモノマー(I)及び(II)及び/又は1つ以上のモノマー(III)を使用して実施してもよい。
(Additive (B))
In the additive (B), the vinyl ester is preferably of the formula CH 2 = CR 1 OOCR 2 (I) (wherein R 1 represents a hydrogen atom or a methyl group, R 2 represents 1 to 4 carbon atoms). Represents an alkyl group having). More preferably, the vinyl ester is vinyl acetate.
The copolymer includes a terpolymer, which is a terpolymer of ethylene, the vinyl ester and a second different vinyl ester having an alkyl group containing 5 to 15 carbon atoms. The second vinyl ester, when used, is preferably CH 2 = CR 3 OOCR 4 (II) (wherein R 3 represents a hydrogen atom or a methyl group, and R 4 is 5 or more, for example, 5 to 15 Represents an alkyl group having carbon atoms, and is preferably a branched alkyl group having 7 to 15 carbon atoms. By way of example, the second vinyl ester may be vinyl 2-ethylhexanoate, vinyl neodecanoate or vinyl octanoate.
As used herein, the term “terpolymer” means that the polymer has at least three different repeating units, ie derived from at least three different monomers, namely ethylene, monomer (I) and monomer (II). Request. The term includes polymers that can be derived from four or more monomers, for example, a polymer may include units that can be derived from two or more monomers (I) and (II), and / or the formula CH 2 = CR 1 OOCR. 5 (III) wherein R 5 represents a hydrocarbyl group having 5 or more carbon atoms, other than those defined by R 4 , may be included.
Thus, the method of the present invention may be carried out using two or more monomers (I) and (II) and / or one or more monomers (III).

本明細書で使用される「ヒドロカルビル」という用語は、分子の残りの部分に直接結合した炭素原子を有し、かつ、炭化水素の性質を有するか、又は炭化水素の性質が支配的である基を意味する。これらの中でも、炭化水素基としては、脂肪族(例えば、アルキル)基、脂環式(例えば、シクロアルキル)基、芳香族基、脂肪族及び脂環式置換芳香族及び脂環式基などが挙げられる。脂肪族基は、有利には飽和である。これらの基は、非炭化水素置換基を含んでもよいが、但し、その存在により基の炭化水素の性質が支配的であることを変えない。その例としては、2-ケトプロピル、エトキシエチル及びプロポキシプロピルなどが挙げられる。また、前記基は、炭素原子で構成される鎖又は環の炭素以外の原子を含んでもよい。この点で好ましい原子としては、例えば窒素、硫黄、好ましくは酸素が挙げられる。有利には、ヒドロカルビル基は、30個以下、好ましくは15個以下、より好ましくは10個以下、最も好ましくは8個以下の炭素原子を含む。
また、式-CH2-CHOH-(IV)の単位をポリマー内に含んでもよい。また、式C(CH3)(CH2R7)=CHR8(V)(R7及びR8は、それぞれ独立に水素又は4個以下の炭素原子を有するアルキル基を表す)のモノマーを使用してもよく、有利にはモノマー(V)はイソブチレン、2-メチルブタ-2-エン又は2-メチルペンタ-2-エンから誘導される。
好ましくは、コポリマー(B)の数平均分子量(Mn)は、2000〜10000の範囲であり、より好ましくは3000〜8000の範囲であり、最も好ましくは4000〜7000の範囲である。本明細書において、Mnは、ポリスチレン標準の、GPCによって測定された値を意味する。
好ましくは、コポリマー(B)の枝分かれ度は、100メチレン単位当たり2〜10個、例えば3〜9個、例えば4〜8個のメチル基である。ポリマーの枝分かれ度は、NMRによって測定し、アルキル基におけるメチル及びメチレン基の数を補正した場合の100メチレン単位当たりのメチル基の数である。参照は、枝分かれ度の計算の例について、欧州特許出願公開第1007606号明細書の図1及びその記載に対してなされる。
また、(B)が2つ以上のポリマーの混合物を含むことは本発明の範囲内である。
As used herein, the term “hydrocarbyl” refers to a group having a carbon atom directly attached to the rest of the molecule and having hydrocarbon properties or predominantly hydrocarbon properties. Means. Among these, hydrocarbon groups include aliphatic (eg, alkyl) groups, alicyclic (eg, cycloalkyl) groups, aromatic groups, aliphatic and alicyclic substituted aromatic and alicyclic groups, and the like. Can be mentioned. The aliphatic group is advantageously saturated. These groups may contain non-hydrocarbon substituents, provided that their presence does not change the predominant hydrocarbon nature of the group. Examples thereof include 2-ketopropyl, ethoxyethyl and propoxypropyl. The group may contain atoms other than carbon in a chain or ring composed of carbon atoms. Preferred atoms in this respect include, for example, nitrogen, sulfur, preferably oxygen. Advantageously, the hydrocarbyl group contains no more than 30, preferably no more than 15, more preferably no more than 10 and most preferably no more than 8 carbon atoms.
The unit of formula —CH 2 —CHOH— (IV) may also be included in the polymer. In addition, a monomer of the formula C (CH 3 ) (CH 2 R 7 ) = CHR 8 (V) (R 7 and R 8 each independently represents hydrogen or an alkyl group having 4 or less carbon atoms) is used. Advantageously, the monomer (V) is preferably derived from isobutylene, 2-methylbut-2-ene or 2-methylpent-2-ene.
Preferably, the number average molecular weight (Mn) of the copolymer (B) is in the range of 2000-10000, more preferably in the range of 3000-8000, and most preferably in the range of 4000-7000. In this specification, Mn means the value of polystyrene standard measured by GPC.
Preferably, the degree of branching of the copolymer (B) is 2 to 10, for example 3 to 9, for example 4 to 8, methyl groups per 100 methylene units. The degree of branching of the polymer is measured by NMR and is the number of methyl groups per 100 methylene units when the number of methyl and methylene groups in the alkyl group is corrected. Reference is made to FIG. 1 and its description of EP 1007606 for an example of calculating the degree of branching.
It is also within the scope of the present invention that (B) comprises a mixture of two or more polymers.

(添加剤(C))
これは、技術的に知られており、例えば米国特許出願公開第2004/0065004号明細書に記載されているアルキルフェノールアルデヒド樹脂のような低分子量フェノール樹脂である。アルキル基は、1〜50個、好ましくは1〜20個、特に4〜12個の炭素原子を有する。アルキル基は、好ましくはn-、イソ及びtert-ブチル;n-及びイソペンチル;n-及びイソヘキシル;n-及びイソオクチル;n-及びイソノニル;n-及びイソデシル;n-及びイソドデシル;及びオクタデシルである。アルデヒドは、好ましくは脂肪族アルデヒドであり、好ましくはホルムアルデヒドである。樹脂の分子量は400〜10000g/モルであり、好ましくは400〜5000g/モルである。
(C)の別の例として、技術的に公知であり、例えば欧州特許出願公開第1482024号明細書に記載されているアルキル(p-ヒドロキシベンゾアート)-アルデヒドポリマー縮合生成物のようなフェノールアルデヒド樹脂が挙げられる。好ましくは、脂肪族アルデヒド又はケトン又は反応性が同等のものと、(i)p-ヒドロキシ安息香酸の直鎖又は分枝鎖C1-C7アルキルエステル、又は(ii)p-ヒドロキシ安息香酸の分枝鎖C8-C16アルキルエステル、又は(iii)p-ヒドロキシ安息香酸の長鎖C8-C18アルキルエステルの混合物(アルキルの少なくとも1つが分岐している)のいずれかとの反応によって形成されるものである。
アルデヒドは、好ましくはホルムアルデヒドである。分枝アルキル基は、好ましくは2-エチルヘキシル又はイソデシルである。一般に、分枝エステルと他のエステルとのモル比は、5:1〜1:5の範囲であってもよい。ポリマー縮合生成物の数平均分子量は、500〜5000の範囲であり、好ましくは1000〜3000の範囲であり、より好ましくは1000〜2000の範囲である。
添加剤(B)及び(C)の質量:質量比は、例えば40:1〜1:20、例えば30:1〜1:1の範囲であってもよい。
(Additive (C))
This is known in the art and is a low molecular weight phenolic resin such as, for example, the alkylphenol aldehyde resins described in US 2004/0065004. The alkyl group has 1 to 50, preferably 1 to 20, especially 4 to 12 carbon atoms. Alkyl groups are preferably n-, iso and tert-butyl; n- and isopentyl; n- and isohexyl; n- and isooctyl; n- and isononyl; n- and isodecyl; n- and isododecyl; The aldehyde is preferably an aliphatic aldehyde, preferably formaldehyde. The molecular weight of the resin is 400 to 10000 g / mol, preferably 400 to 5000 g / mol.
As another example of (C), phenol aldehydes known in the art, such as alkyl (p-hydroxybenzoate) -aldehyde polymer condensation products described in EP-A-1482024, for example. Resin. Preferably, an aliphatic aldehyde or ketone or equivalent is equivalent to (i) a linear or branched C 1 -C 7 alkyl ester of p-hydroxybenzoic acid, or (ii) p-hydroxybenzoic acid Formed by reaction with either a branched C 8 -C 16 alkyl ester, or (iii) a mixture of long chain C 8 -C 18 alkyl esters of p-hydroxybenzoic acid, where at least one of the alkyls is branched It is what is done.
The aldehyde is preferably formaldehyde. The branched alkyl group is preferably 2-ethylhexyl or isodecyl. In general, the molar ratio of branched ester to other ester may range from 5: 1 to 1: 5. The number average molecular weight of the polymer condensation product is in the range of 500 to 5000, preferably in the range of 1000 to 3000, and more preferably in the range of 1000 to 2000.
The mass: mass ratio of additives (B) and (C) may be, for example, in the range of 40: 1 to 1:20, for example 30: 1 to 1: 1.

(追加の添加剤)
燃料油組成物は、添加剤(B)及び(C)に加えて、それら以外の1つ以上の添加剤を含んでもよい。それらの存在は、性能のさらなる改善をもたらす場合がある。
追加の添加剤の好ましい例として、以下のものが挙げられる。
(D)1級、2級又は3級ヒドロカルビルアミン又は4級ヒドロカルビルアンモニウム塩(ヒドロカルビル基のうち少なくとも1つは、8〜40個の炭素原子を含む。)から誘導される1つ以上の置換基を有する油溶性極性窒素化合物。油溶性極性窒素化合物は、一般に燃料中のワックス結晶成長抑制剤として作用できるものであり、例えば以下の化合物のうち1つ以上を含む。
少なくとも1モルのヒドロカルビル置換アミンと、1〜4個のカルボン酸基又はその無水物を有する1モルのヒドロカルビル酸との反応によって形成されるアミン塩及び/又はアミド(置換基は式-NR13R14(式中、R13は8〜40個の炭素原子を含むヒドロカルビル基を表し、R14は水素又はR13を表すが、R13及びR14は同じであっても、又は異なっていてもよく、前記置換基は化合物のアミン塩及び/又はアミド基の一部を構成する)。
(Additional additive)
The fuel oil composition may contain one or more additives in addition to the additives (B) and (C). Their presence may lead to further improvements in performance.
Preferred examples of the additional additive include the following.
(D) one or more substituents derived from a primary, secondary or tertiary hydrocarbylamine or quaternary hydrocarbylammonium salt (at least one of the hydrocarbyl groups contains 8 to 40 carbon atoms). An oil-soluble polar nitrogen compound. The oil-soluble polar nitrogen compound can generally act as a wax crystal growth inhibitor in fuel and includes, for example, one or more of the following compounds.
Amine salts and / or amides formed by reaction of at least 1 mole of hydrocarbyl-substituted amine with 1 mole of hydrocarbyl acid having 1 to 4 carboxylic acid groups or anhydrides (substituent is of the formula —NR 13 R 14 wherein R 13 represents a hydrocarbyl group containing 8 to 40 carbon atoms and R 14 represents hydrogen or R 13 , R 13 and R 14 may be the same or different. Often, the substituents constitute part of the amine salt and / or amide group of the compound).

合計30〜300個、好ましくは50〜150個の炭素原子を含むエステル/アミドを用いてもよい。これらの窒素化合物は、米国特許第4211534号明細書に記載されている。適したアミンは、主にC12-C401級、2級、3級又は4級アミン又はその混合物であるが、得られる窒素化合物が油溶性であるならば、より短い鎖のアミンを使用してもよく、通常合計約30〜300個の炭素原子を含む。窒素化合物は、好ましくは少なくとも1つの直鎖C8-C40、好ましくはC14-C24アルキル部分を含む。
適したアミンとしては、1級、2級、3級又は4級が挙げられるが、好ましくは2級である。3級及び4級アミンのみアミン塩を形成する。アミンの例としては、テトラデシルアミン、ココアミン、及び水素化タローアミンなどが挙げられる。2級アミンの例としては、ジオクタデシルアミン(diotacedyl amine)及びメチルベヘニルアミンなどが挙げられる。また、アミン混合物は、天然物質から誘導されるものなどが適している。好ましいアミンは、2級水素化タローアミンであり、そのアルキル基は、約4%のC14、約31%のC16及び59%のC18で構成される水素化タロー脂から誘導される。
Esters / amides containing a total of 30 to 300, preferably 50 to 150 carbon atoms may be used. These nitrogen compounds are described in US Pat. No. 4211534. Suitable amines are primarily C 12 -C 40 primary, secondary, tertiary or quaternary amines or mixtures thereof, but shorter chain amines are used if the resulting nitrogen compound is oil soluble. And usually contains a total of about 30 to 300 carbon atoms. The nitrogen compound preferably comprises at least one linear C 8 -C 40 , preferably C 14 -C 24 alkyl moiety.
Suitable amines include primary, secondary, tertiary or quaternary, preferably secondary. Only tertiary and quaternary amines form amine salts. Examples of amines include tetradecylamine, cocoamine, and hydrogenated tallow amine. Examples of secondary amines include dioctacedyl amine and methylbehenylamine. Also suitable as the amine mixture are those derived from natural substances. A preferred amine is a secondary hydrogenated tallow amine, the alkyl group of which is derived from a hydrogenated tallow fat composed of about 4% C 14 , about 31% C 16 and 59% C 18 .

前記窒素化合物を調製するのに好適なカルボン酸及びその無水物の例としては、エチレンジアミン四酢酸、及び環状骨格をベースとするカルボン酸、例えばシクロヘキサン-1,2-ジカルボン酸、シクロヘキセン-1,2-ジカルボン酸、シクロペンタン-1,2-ジカルボン酸及びナフタレンジカルボン酸、及びジアルキルスピロビスラクトンなどの1,4-ジカルボン酸などが挙げられる。一般に、これらの酸は、環状部分に約5〜13個の炭素原子を有する。本発明で有用な好ましい酸は、ベンゼンジカルボン酸、例えばフタル酸、イソフタル酸、及びテレフタル酸である。フタル酸及びその無水物は、特に好ましい。特に好ましい化合物は、1モルの無水フタル酸と2モルの2水素化タローアミンとの反応によって形成されるアミド-アミン塩である。別の好ましい化合物は、このアミド-アミン塩を脱水して形成されるジアミドである。
その他の例は、長鎖アルキル又はアルキレン置換ジカルボン酸誘導体、例えば置換コハク酸のモノアミドのアミン塩であり、その例は技術的に公知であり、例えば米国特許第4147520号明細書に記載されている。適したアミンは上述のものである。
その他の例は、縮合物、例えば欧州特許出願公開第327427号明細書に記載されるものである。
Examples of suitable carboxylic acids and anhydrides for preparing the nitrogen compounds include ethylenediaminetetraacetic acid and carboxylic acids based on cyclic skeletons such as cyclohexane-1,2-dicarboxylic acid, cyclohexene-1,2 -1,4-dicarboxylic acid such as dicarboxylic acid, cyclopentane-1,2-dicarboxylic acid and naphthalenedicarboxylic acid, and dialkyl spirobislactone. Generally, these acids have about 5 to 13 carbon atoms in the cyclic portion. Preferred acids useful in the present invention are benzene dicarboxylic acids such as phthalic acid, isophthalic acid, and terephthalic acid. Phthalic acid and its anhydride are particularly preferred. A particularly preferred compound is an amide-amine salt formed by the reaction of 1 mole of phthalic anhydride and 2 moles of dihydrogenated tallow amine. Another preferred compound is a diamide formed by dehydrating the amide-amine salt.
Other examples are long chain alkyl or alkylene substituted dicarboxylic acid derivatives, such as amine salts of monoamides of substituted succinic acids, examples of which are known in the art and are described, for example, in US Pat. No. 4,147,520. . Suitable amines are those mentioned above.
Other examples are condensates such as those described in EP-A-327427.

さらに追加の添加剤としては、以下のものが挙げられる。
(E)10〜30個の炭素原子を有するヒドロカルビル基を含む分枝がポリマー骨格、例えばマレアート、フマラート又はイタコナートポリマー及びコポリマーからのペンダントであるコームポリマー;
(F)少なくとも1つの結晶性ブロック(線状ジエンの端と端とが接する重合によって得られる)及び少なくとも1つの非結晶性ブロック(線状ジエンの1,2-配置重合、分枝ジエンの重合、又は前記重合の混合によって得られる)を含むような、水素化ブロックジエンポリマー;
(G)環系を含む化合物;
(H)炭化水素ポリマー;及び
(I)ポリオキシアルキレン化合物。
技術文献、例えば国際公開第96/28523号パンフレットには、前記添加剤のさらなる説明が含まれている。
技術的に公知であるような1つ以上の他の共添加剤(co-additives)を用いてもよい。そのようなその他の共添加剤の例として、以下のものが挙げられる:洗浄剤、特に排ガス還元剤(emission reducers)、貯蔵安定剤、抗酸化剤、腐食防止剤、デハザーズ(dehazers)、解乳化剤、消泡剤、セタン価向上剤、共溶媒、パッケージ相溶化剤及び潤滑添加剤。
Additional additives include the following.
(E) a comb polymer in which the branches containing hydrocarbyl groups having 10 to 30 carbon atoms are pendant from a polymer backbone, such as maleate, fumarate or itaconate polymers and copolymers;
(F) at least one crystalline block (obtained by end-to-end polymerization of linear diene) and at least one non-crystalline block (1,2-configuration polymerization of linear diene, polymerization of branched diene) Hydrogenated block diene polymers such as, or obtained by mixing of said polymerizations;
(G) a compound containing a ring system;
(H) a hydrocarbon polymer; and (I) a polyoxyalkylene compound.
Technical literature, for example WO 96/28523, contains further explanation of the additives.
One or more other co-additives as known in the art may be used. Examples of such other co-additives include the following: cleaning agents, especially emission reducers, storage stabilizers, antioxidants, corrosion inhibitors, dehazers, demulsifiers , Antifoams, cetane improvers, co-solvents, package compatibilizers and lubricant additives.

(組成物の調製)
好適な溶媒と混合して本発明の添加剤を含む濃厚物は、前記添加剤を燃料油に添加する手段として都合がよく、前記添加は技術的に公知の方法によって行ってもよい。また、濃厚物は、必要に応じてその他の添加剤を含んでもよく、活性成分として表して、好ましくは3〜75質量%、より好ましくは3〜60質量%、最も好ましくは10〜50質量%の添加剤(好ましくは、油に溶ける)を含む。溶媒の例としては、炭化水素溶媒、例えばナフサ、灯油、ディーゼル及び暖房用オイルのような石油留分;芳香族留分、例えば「SOLVESSO」の商品名で市販されているもののような芳香族炭化水素;アルコール及び/又はエステル;及びヘキサン及びペンタンのようなパラフィン系炭化水素及びイソパラフィンなどの有機溶媒である。溶媒は、もちろん添加剤及び燃料油とのその相溶性を考慮して、選択されなければならない。本発明の燃料油組成物は、燃料油の質量を基準として、有利には0.0005〜1質量%、より有利には0.001〜0.1質量%、好ましくは0.01〜0.06質量%の割合で添加剤を含む。
(Preparation of composition)
Concentrates containing the additive of the present invention mixed with a suitable solvent are convenient as a means of adding the additive to the fuel oil, and the addition may be performed by methods known in the art. Further, the concentrate may contain other additives as necessary, and is expressed as an active ingredient, preferably 3 to 75% by mass, more preferably 3 to 60% by mass, most preferably 10 to 50% by mass. Additional additives (preferably soluble in oil). Examples of solvents include hydrocarbon solvents such as petroleum fractions such as naphtha, kerosene, diesel and heating oil; aromatic fractions such as those aromatic hydrocarbons such as those marketed under the name “SOLVESSO”. Hydrogen; alcohols and / or esters; and organic solvents such as paraffinic hydrocarbons such as hexane and pentane and isoparaffins. The solvent must of course be selected taking into account its compatibility with the additive and fuel oil. The fuel oil composition of the present invention comprises an additive in a proportion of advantageously 0.0005 to 1% by weight, more advantageously 0.001 to 0.1% by weight, preferably 0.01 to 0.06% by weight, based on the weight of the fuel oil. .

(発明の実施例)
特許請求の範囲を制限することを意図しない以下の実施例で、本発明を説明する。
(Embodiment of the invention)
The invention is illustrated in the following examples, which are not intended to limit the scope of the claims.

(添加剤)
実施例において、以下の添加剤を単独で又は混合物で組み合わせて使用した。
(B)アレスター及び核剤の3:1(重量:重量)混合物の形態のエチレン-酢酸ビニルコポリマー低温流動性向上剤(「EVA」);
(C)アルキル(p-ヒドロキシベンゾアート)-ホルムアルデヒド縮合コポリマー(「HBFC」);
(D)極性窒素化合物の形態の市販のワックス分散剤(「WASA」);
(E)C14フマラート-酢酸ビニルコームコポリマー(「FVA」)。
(Additive)
In the examples, the following additives were used alone or in combination in a mixture.
(B) an ethylene-vinyl acetate copolymer cold flow improver ("EVA") in the form of a 3: 1 (weight: weight) mixture of arrester and nucleating agent;
(C) alkyl (p-hydroxybenzoate) -formaldehyde condensation copolymer ("HBFC");
(D) a commercially available wax dispersant ("WASA") in the form of a polar nitrogen compound;
(E) C14 fumarate-vinyl acetate comb copolymer (“FVA”).

(燃料)
残留燃料油の添加を含み、重油Aで示される中間留出燃料を実施例で用いた。前記燃料は以下の性質を有していた。

Figure 2007238945
(fuel)
A middle distillate fuel designated heavy oil A was used in the examples, including the addition of residual fuel oil. The fuel had the following properties.
Figure 2007238945

(燃料油組成物及びテスト)
上記添加剤の1つ以上を上記燃料に混合していくつかの燃料油組成物を供給した。
各組成物のサンプルを、暖房用オイル組成物の使用条件、すなわち遅い冷却速度をシミュレートするように設計したリグテストに供し、次いで組成物をボイラーに供給する前に、メッシュフィルターを通した。
テスト条件は以下のとおりであった。
a)冷却速度:1℃/時間
b)油組成物サンプルの体積:200ml
c)減圧:600mmHg
d)フィルターメッシュサイズ:150ml
結果を、指定温度で、サンプル体積のすべてがフィルターを通過する時間を秒で表す。通常、180秒以内の時間が合格とみなされ、15秒未満は良好とみなされ、180秒よりも長い時間は不合格とみなされる。結果を下記表1にまとめる。目標のリグ温度は-4℃であり、添加剤処理率は300ppm(質量)であった。
比較目的のための参照例は「比較例1」で示す。本発明の実施例は数字によって示される。また、「コントロール」で示される添加剤を含まない(すなわち、対照)燃料についての結果も示す。
(Fuel oil composition and test)
One or more of the above additives were mixed with the fuel to provide several fuel oil compositions.
Samples of each composition were subjected to a rig test designed to simulate the conditions of use of the heating oil composition, i.e. slow cooling rate, and then passed through a mesh filter before feeding the composition to the boiler.
The test conditions were as follows:
a) Cooling rate: 1 ° C./hour b) Volume of oil composition sample: 200 ml
c) Depressurization: 600mmHg
d) Filter mesh size: 150ml
Results are expressed in seconds at the specified temperature, all of the sample volume passes through the filter. Usually, a time within 180 seconds is considered acceptable, a time less than 15 seconds is considered good, and a time longer than 180 seconds is considered unacceptable. The results are summarized in Table 1 below. The target rig temperature was −4 ° C., and the additive treatment rate was 300 ppm (mass).
A reference example for comparison purposes is indicated by “Comparative Example 1”. Embodiments of the invention are indicated by numbers. Also shown are the results for fuels that do not contain the additive indicated by “control” (ie, control).

Figure 2007238945
Figure 2007238945

結果は、添加剤(C)の存在が添加剤(B)単独によって与えられるよりも添加剤(B)の性能を改善する。また、添加剤(E)の使用は安定性の問題を生じるが、添加剤(D)及び(E)の存在は、テストにおいて性能に影響を与える場合がある。   The result improves the performance of additive (B) than the presence of additive (C) is provided by additive (B) alone. Also, the use of additive (E) causes stability problems, but the presence of additives (D) and (E) may affect performance in testing.

Claims (10)

(A)0.1質量%よりも多い残留炭素(ASTM D189による測定)を有する過半量の中間留分燃料油;及び少割合の以下の各添加剤を含む燃料油組成物:
(B)1つ以上の、エチレン及び1〜18個の炭素原子を含むアルキル基を有するビニルエステルのコポリマー;及び
(C)1つ以上の、分子量が400〜10,000g/モルであるフェノール樹脂。
(A) a fuel oil composition comprising a majority of middle distillate fuel oil having greater than 0.1% by weight residual carbon (as measured by ASTM D189); and a small proportion of each of the following additives:
(B) a copolymer of one or more vinyl esters having ethylene and an alkyl group containing 1 to 18 carbon atoms; and (C) one or more phenolic resins having a molecular weight of 400 to 10,000 g / mol.
残留炭素が0.2〜0.5質量%の範囲である、請求項1記載の組成物。   The composition of claim 1, wherein the residual carbon is in the range of 0.2 to 0.5 wt%. 燃料油が2〜10質量%の残留燃料油を含む、請求項1又は2記載の組成物。   The composition according to claim 1 or 2, wherein the fuel oil comprises 2 to 10% by weight of residual fuel oil. コポリマー(B)において、ビニルエステルが式CH2=CR1OOCR2(式中、R1は水素原子又はメチル基を表し、R2は1〜4個の炭素原子を有するアルキル基を表す)を有する、請求項1〜3のいずれか1項記載の組成物。 In the copolymer (B), the vinyl ester has the formula CH 2 = CR 1 OOCR 2 (wherein R 1 represents a hydrogen atom or a methyl group, and R 2 represents an alkyl group having 1 to 4 carbon atoms). The composition of any one of Claims 1-3 which has. コポリマー(B)がエチレン、請求項4において定義されるビニルエステル及び5〜15個の炭素原子を含むアルキル基を有する第2の異なるビニルエステルのターポリマーである、請求項1〜4のいずれか1項記載の組成物。   5. Copolymer (B) is a terpolymer of ethylene, a vinyl ester as defined in claim 4 and a second different vinyl ester having an alkyl group containing 5 to 15 carbon atoms. A composition according to claim 1. 樹脂(C)がアルキルフェノール-アルデヒド樹脂であり、アルキル基が1〜50個の炭素原子を有する、請求項1〜5のいずれか1項記載の組成物。   The composition according to any one of claims 1 to 5, wherein the resin (C) is an alkylphenol-aldehyde resin and the alkyl group has 1 to 50 carbon atoms. 樹脂(C)がアルキル(p-ヒドロキシベンゾアート)-アルデヒドポリマー縮合物である、請求項6記載の組成物。   The composition according to claim 6, wherein the resin (C) is an alkyl (p-hydroxybenzoate) -aldehyde polymer condensate. 樹脂(C)が4-ヒドロキシ安息香酸のエステルとのホルムアルデヒド縮合コポリマーである、請求項7記載の組成物。   8. A composition according to claim 7, wherein the resin (C) is a formaldehyde condensation copolymer with an ester of 4-hydroxybenzoic acid. さらに、添加剤として、
(D)1級、2級又は3級ヒドロカルビルアミン又は4級ヒドロカルビルアンモニウム塩から誘導される1つ以上の置換基を有する油溶性極性窒素化合物であって、ヒドロカルビル基の少なくとも1つが8〜40個の炭素原子を含む化合物を含む、請求項1〜7のいずれか1項記載の組成物。
In addition, as an additive
(D) An oil-soluble polar nitrogen compound having one or more substituents derived from a primary, secondary or tertiary hydrocarbylamine or quaternary hydrocarbyl ammonium salt, wherein at least one hydrocarbyl group is 8 to 40 The composition of any one of Claims 1-7 containing the compound containing these carbon atoms.
添加剤が、燃料油の質量を基準として、0.1〜0.3質量%の範囲で存在する、請求項1〜9のいずれか1項記載の組成物。   The composition according to any one of claims 1 to 9, wherein the additive is present in a range of 0.1 to 0.3% by mass, based on the mass of the fuel oil.
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