JP2005538204A - Diesel fuel composition containing components based on biological raw materials obtained by hydrogenating and decomposing fatty acids - Google Patents

Diesel fuel composition containing components based on biological raw materials obtained by hydrogenating and decomposing fatty acids Download PDF

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JP2005538204A
JP2005538204A JP2004533535A JP2004533535A JP2005538204A JP 2005538204 A JP2005538204 A JP 2005538204A JP 2004533535 A JP2004533535 A JP 2004533535A JP 2004533535 A JP2004533535 A JP 2004533535A JP 2005538204 A JP2005538204 A JP 2005538204A
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fuel composition
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fish
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ヤックラ、ユハ
アールト、ペッカ
ニエミ、ベサ
キースキ、ウッラ
ニッコネン、ヨウコ
ミッコネン、セッポ
ピーライネン、オウチ
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フォータム オイル オサケ ユキチュア
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Abstract

本発明はディーゼルエンジン用燃料組成物に関する。この燃料組成物は、植物および/または動物および/または魚を起源とする生物学的原材料から調製される成分または成分の混合物を0.1〜99容量%含む。この燃料組成物は、酸素を含む成分を0〜20容量%含む。両成分は、フィッシャー−トロプシュ工程からの粗油および/または画分にもとづくディーゼル成分と混合される。The present invention relates to a fuel composition for a diesel engine. The fuel composition comprises 0.1 to 99% by volume of a component or mixture of components prepared from biological raw materials originating from plants and / or animals and / or fish. This fuel composition contains 0 to 20% by volume of oxygen-containing components. Both components are mixed with diesel components based on crude oil and / or fractions from the Fischer-Tropsch process.

Description

本発明は、植物油および/または動物脂質および/または魚油にもとづく成分、フィッシャー−トロプシュ(Fischer-Tropsch)工程からの粗油および/または画分にもとづくディーゼル成分、ならびに任意に酸素を含む成分を含むディーゼルエンジン用燃料組成物に関する。   The present invention includes components based on vegetable and / or animal lipids and / or fish oil, diesel components based on crude oil and / or fractions from the Fischer-Tropsch process, and optionally oxygen-containing components. The present invention relates to a fuel composition for a diesel engine.

現在のところ、ディーゼルエンジン用燃料としては、粗油由来の成分を主に含む燃料が使用されている。京都の気候協定(the climate agreement)の目的は、大気、すなわち気候に対する人間活動による悪影響を排除することである。EUは、1990年レベルを基準にして2010年までに、二酸化炭素、メタンおよびその他の温室ガスの放出を8%減少させることに同意している。EU農業政策の課題のひとつが、農業による過剰生産物の使い道を見つけること、および、燃料の自給自足を進めることである。したがって、2005年に消費される石油およびディーゼル燃料の少なくとも2%を生物学的起源のものにすべきとの要求が盛り込まれているEU指令書(directive)が作成されている。この指令書の要求の1つが、生物成分の割合を2010年までに約6%にまで増加させることと予期される。この指令書は、近い将来、EUすべての国において有効となるであろう。   At present, fuels mainly containing components derived from crude oil are used as fuels for diesel engines. The purpose of the climate agreement in Kyoto is to eliminate the negative effects of human activities on the atmosphere, or climate. The EU has agreed to reduce carbon dioxide, methane and other greenhouse gas emissions by 8% by 2010 relative to the 1990 level. One of the challenges of EU agricultural policy is to find ways to use excess products from agriculture and to promote fuel self-sufficiency. Thus, an EU directive has been created that includes a requirement that at least 2% of the petroleum and diesel fuel consumed in 2005 should be of biological origin. One of the requirements of this directive is expected to increase the proportion of biological components to about 6% by 2010. This directive will be effective in all EU countries in the near future.

現在のところ、燃料における生物学的起源のもっとも一般的な成分としては、ナタネ油(rapeseed oil)メチルエステル(RMEという)である。RMEは、そのままか、または燃料との混合物としてのいずれかで使用される。RMEの欠点は、ディーゼル燃料との混和性に乏しく、そして、従来のディーゼル燃料(EN590)と比較して、とくに低温条件下での保存安定性に乏しく、かつ低温時の性能が劣ることである。さらに、それはエンジンの汚れの原因となり、またチッ素酸化物(NOx)の放出を増加させる。RMEの生産工程の副産物はグリセロールである。これは、大量の生成物が生産されるときに問題となり得る。その他の植物油のエステルも同様の方法で生産され得、そして脂肪酸のメチルエステルはFAME(脂肪酸メチルエステル)として一般に知られている。これらのFAMEは、ナタネ油メチルエステルと同じ用途に使用され得る。しかし、FAMEは、ディーゼル燃料の品質、とくに低温時の性能に関してマイナスの効果を有し、さらに、燃料におけるFAMEの使用は、チッ素酸化物の放出を増加させる。場合によっては、FAMEおよびRMEは、低温下でエンジンを操縦することによって煙が発生したり、粒子の放出が多くなったりする原因となる。 At present, the most common component of biological origin in fuel is rapeseed oil methyl ester (referred to as RME). The RME is used either as it is or as a mixture with fuel. Disadvantages of RME are poor miscibility with diesel fuel, and poor storage stability especially under low temperature conditions and poor performance at low temperatures compared to conventional diesel fuel (EN590). . In addition, it causes engine fouling and increases nitrogen oxide (NO x ) emissions. A by-product of the RME production process is glycerol. This can be a problem when large quantities of product are produced. Other vegetable oil esters can be produced in a similar manner, and the methyl esters of fatty acids are commonly known as FAME (fatty acid methyl esters). These FAMEs can be used for the same applications as rapeseed oil methyl ester. However, FAME has a negative effect on the quality of diesel fuel, especially at low temperatures, and the use of FAME in the fuel increases the emission of nitrogen oxides. In some cases, FAME and RME can cause smoke or increased particle emissions when the engine is operated at low temperatures.

植物油および動物脂質は処理により、エステルおよび/または脂肪酸構造が分解され、炭化水素鎖の二重結合が飽和して、出発原料の量に対して約80〜85%のn−パラフィン生成物が得られる。この生成物は、ディーゼル燃料と直接混合され得るが、そのようにして製造された燃料は、低温時の性能が劣るという問題がある。さらに、炭素数が多い脂肪酸を有するn−パラフィンは、凝固点が高く(代表的には約+10℃)蝋質である。したがって、少なくとも低温時での、これらの化合物のディーゼル燃料における使用は、制限される。   Treatment of vegetable oils and animal lipids results in degradation of the ester and / or fatty acid structure and saturation of the hydrocarbon chain double bonds to yield about 80-85% n-paraffin product relative to the amount of starting material. It is done. This product can be mixed directly with diesel fuel, but the fuel so produced has the problem of poor performance at low temperatures. Furthermore, n-paraffins having fatty acids with high carbon numbers have a high freezing point (typically about + 10 ° C.) and are waxy. Therefore, the use of these compounds in diesel fuel, at least at low temperatures, is limited.

国際公開2001/049812号パンフレットは、イソ−パラフィンとn−パラフィンのモル比が少なくとも21:1であるディーゼル燃料の製造方法を開示している。この方法において、C10−パラフィンを50%以上含む供給原料は、異性化反応帯において触媒と接触される。 WO 2001/049812 discloses a method for producing diesel fuel in which the molar ratio of iso-paraffin to n-paraffin is at least 21: 1. In this process, a feedstock containing 50% or more C 10 -paraffin is contacted with the catalyst in the isomerization reaction zone.

国際公開2001/012581号パンフレットは、生物学的ディーゼル燃料として有用であるメチルエステルの製造方法を開示している。ここで、脂肪酸とトリグリセリドの混合物は1相でエステル化される。この方法において、溶液は、溶液の沸点以下の温度で、脂肪酸、トリグリセリド、アルコール、酸触媒および共溶媒から形成される。共溶媒が使用されて単一相となり、ついで、その溶液は脂肪酸の酸触媒エステル化が起こるのに充分な時間維持される。その後、酸触媒は中和され、塩基触媒を添加してトリグリセリドがエステル交換される。そして、最終的にエステルは溶液から分離される。したがって、グリセロール含量が0.4重量%未満のエステルを含むバイオ燃料が得られる。   WO 2001/012581 discloses a process for producing methyl esters that are useful as biological diesel fuels. Here, the mixture of fatty acid and triglyceride is esterified in one phase. In this method, the solution is formed from fatty acids, triglycerides, alcohols, acid catalysts and cosolvents at temperatures below the boiling point of the solution. A co-solvent is used to form a single phase, and then the solution is maintained for a time sufficient for acid-catalyzed esterification of the fatty acid to occur. Thereafter, the acid catalyst is neutralized, and the base catalyst is added to transesterify the triglyceride. Finally, the ester is separated from the solution. A biofuel containing an ester having a glycerol content of less than 0.4% by weight is thus obtained.

米国特許第6,174,501号明細書は、生物学的起源の酸化ディーゼル燃料の製造方法を公開している。この酸化生物学的ディーゼル燃料は、エステル交換トリグリセリドの混合物を含む。   US Pat. No. 6,174,501 discloses a method for producing oxidized diesel fuel of biological origin. This oxidized biological diesel fuel comprises a mixture of transesterified triglycerides.

フィンランド特許第100248号明細書は、植物油からの中蒸留物(middle distillate)の2段階製造方法を開示している。この製造方法は、植物油の脂肪酸、またはトリグリセリドを水素化してn−パラフィンを得て、ついで、そのn−パラフィンを異性化して分岐鎖パラフィンを得ることによる。   Finnish patent 100248 discloses a two-stage process for the production of middle distillate from vegetable oil. This production method is based on hydrogenation of a fatty acid or triglyceride of a vegetable oil to obtain n-paraffin, and then isomerization of the n-paraffin to obtain a branched chain paraffin.

人の健康に有害ならびに/または動物、植物および種々の物質に悪影響である量で大気中に存在する任意の気体、液滴および固体粒子は大気汚染物質と考えられる。大気汚染はおもに3つの放出起源(すなわち、工業、エネルギー生産および交通)からもたらされる。   Any gas, droplets and solid particles present in the atmosphere in amounts that are harmful to human health and / or adversely affect animals, plants and various substances are considered air pollutants. Air pollution comes primarily from three emission sources (ie, industry, energy production and traffic).

粒子放出の有害性は、その物質および化合物が重金属およびその他の発ガン性および変異性化合物などを持っていることによって生じる。排気ガス中に存在する粒子は小さく、そのため健康に有害である。   The hazards of particle release arise from the fact that the substances and compounds have heavy metals and other carcinogenic and mutated compounds. The particles present in the exhaust gas are small and therefore harmful to health.

温室ガスは、太陽からの放射の進入を地球に到達させるが、熱放射を地球から宇宙に逃がすことを妨げる。したがって、温室ガスは地球の温暖化に寄与している。もっとも重要な温室ガスの1つに、たとえば、化石燃料の燃焼中に放出される二酸化炭素がある。   Greenhouse gas allows the radiation from the sun to reach the earth, but prevents heat radiation from escaping from the earth into space. Therefore, greenhouse gas contributes to global warming. One of the most important greenhouse gases is, for example, carbon dioxide released during the combustion of fossil fuels.

チッ素酸化物は酸性化化合物である。この酸化は、たとえば、植物を損傷させたり、地表水において種の変化をもたらす可能性がある。チッ素酸化物はまた酸素と反応してオゾンを与える。この現象はとくに都市における空気の質に寄与する。   Nitrogen oxide is an acidifying compound. This oxidation can, for example, damage plants or cause species changes in surface water. Nitrogen oxide also reacts with oxygen to give ozone. This phenomenon especially contributes to air quality in cities.

前記の教示に示したとおり、生物学的起源の成分を含むディーゼルエンジン用の高品質の燃料組成物が必要とされており、また、低温での操作条件下でのディーゼル燃料に対する品質が求められている。さらに、その燃料は先行技術の溶液よりも環境にやさしくなければならない。   As indicated in the above teachings, there is a need for high quality fuel compositions for diesel engines that contain components of biological origin, and there is a need for quality for diesel fuel under low temperature operating conditions. ing. In addition, the fuel must be more environmentally friendly than prior art solutions.

本発明は、生物学的起源の成分を含み、かつ低温条件下でのディーゼル燃料に対する品質要求を備える、環境にやさしいディーゼルエンジン用燃料組成物を提供することを目的とする。   The present invention seeks to provide an environmentally friendly diesel engine fuel composition comprising components of biological origin and having quality requirements for diesel fuel under low temperature conditions.

生物学的起源の成分を含む本発明のディーゼルエンジン用燃料組成物は、植物、動物または魚から得られる生物学的原材料から調製される少なくとも1種類の成分、フィッシャー−トロプシュ工程からの粗油および/または画分にもとづくディーゼル成分ならびに任意に酸素を含む成分からなる。   The diesel engine fuel composition of the present invention comprising components of biological origin comprises at least one component prepared from biological raw materials obtained from plants, animals or fish, crude oil from a Fischer-Tropsch process, and It consists of a diesel component based on the fraction and / or a component optionally containing oxygen.

生物学的起源の成分を含むディーゼルエンジン用燃料組成物の特徴は、添付の特許請求の範囲に示される。   The characteristics of a fuel composition for a diesel engine comprising components of biological origin are set forth in the appended claims.

驚くべきことに、生物学的起源の成分を含む本発明のディーゼル燃料組成物はまた、低温条件下でのディーゼル燃料に対する品質要求を満たすということを見出した。本発明のディーゼル燃料の組成物は、以下のとおりである:
a)植物および/または動物および/または魚を起源とする生物学的原材料から調製される成分または成分の混合物を0.1〜99容量%、好ましくは0.1〜80容量%;
b)脂肪族アルコール(たとえば、メタノールおよびエタノール)、エーテル、脂肪酸エステル(たとえば、メチルエステルおよびエチルエステル)、水、およびそれらを含む混合物からなる群から選択される酸素を含む成分を0〜20容量%;
ここで、成分a)およびb)はエマルジョンとして混合されるか、またはフィッシャー−トロプシュ工程からの粗油および/または画分にもとづくディーゼル成分中に溶解される。
Surprisingly, it has been found that the diesel fuel composition of the present invention comprising components of biological origin also meets the quality requirements for diesel fuel under low temperature conditions. The diesel fuel composition of the present invention is as follows:
a) 0.1 to 99% by volume, preferably 0.1 to 80% by volume, of a component or mixture of components prepared from biological raw materials originating from plants and / or animals and / or fish;
b) 0-20 volumes of an oxygen-containing component selected from the group consisting of aliphatic alcohols (eg, methanol and ethanol), ethers, fatty acid esters (eg, methyl esters and ethyl esters), water, and mixtures containing them. %;
Here, components a) and b) are mixed as emulsions or dissolved in diesel components based on crude oil and / or fractions from the Fischer-Tropsch process.

植物および/または動物および/または魚を起源とする生物学的原材料から調製される成分a)(本明細書において生物学的成分という)は、脂肪酸および/または脂肪酸エステルを水素化および分解して、炭素数が6〜24である炭化水素、代表的には炭素数が12〜24である生成物としてn−パラフィンを得、任意に、炭化水素、代表的にはn−パラフィンを異性化することによってイソ−パラフィンを得ることによって得られる。炭化水素は好ましくは異性化される。   Component a) (referred to herein as a biological component) prepared from biological raw materials originating from plants and / or animals and / or fish, hydrogenates and decomposes fatty acids and / or fatty acid esters. Obtaining n-paraffins as hydrocarbons having 6 to 24 carbon atoms, typically products having 12 to 24 carbon atoms, and optionally isomerizing hydrocarbons, typically n-paraffins To obtain iso-paraffin. The hydrocarbon is preferably isomerized.

植物および/または動物および/または魚を起源とする生物学的原材料は、脂肪酸および/または脂肪酸エステルを含む植物油、動物脂質、魚油およびそれらの混合物からなる群から選択される。適切な材料の例としては、木ベースの脂質および油ならびに他の植物ベースの脂質および油(たとえば、ナタネ油、ナタネ油(colza oil)、カノーラ油、トール油、ヒマワリ油、ダイズ油、アサミ油、オリーブ油、アマニ油、カラシ油、パーム油、ピーナッツ油、ヒマシ油、ココナッツ油ならびに遺伝子操作による品種改良植物に含まれる脂質)、動物ベースの脂質(たとえば、ラード、獣脂、魚油および乳に含まれる脂質)および食品工業の再利用した脂質ならびにそれらの混合物があげられる。   The biological raw material originating from plants and / or animals and / or fish is selected from the group consisting of vegetable oils, animal lipids, fish oils and mixtures thereof containing fatty acids and / or fatty acid esters. Examples of suitable materials include wood-based lipids and oils and other plant-based lipids and oils (eg, rapeseed oil, colza oil, canola oil, tall oil, sunflower oil, soybean oil, assami oil , Olive oil, flaxseed oil, mustard oil, palm oil, peanut oil, castor oil, coconut oil and lipids contained in genetically engineered breeding plants, animal-based lipids (eg lard, tallow, fish oil and milk) Lipids) and reused lipids from the food industry and mixtures thereof.

代表的な植物脂質または動物脂質の基本成分はトリグリセリド、すなわち、グリセロールのトリエステルおよび以下の式Iに示した構造を有する3つの脂肪酸分子である。   The basic components of typical plant or animal lipids are triglycerides, ie, triesters of glycerol and three fatty acid molecules having the structure shown in Formula I below.

Figure 2005538204
Figure 2005538204

(式中、R1、R2およびR3は炭化水素鎖であり、そしてR1、R2およびR3は飽和または不飽和C6−C24アルキル基であってもよい。脂肪酸組成は生物学的原材料の起源が異なると相当変化し得る) Wherein R 1 , R 2 and R 3 are hydrocarbon chains, and R 1 , R 2 and R 3 may be saturated or unsaturated C 6 -C 24 alkyl groups. Can vary considerably with different origins of biological raw materials)

生物学的原材料から調製されるn−パラフィン、イソ−パラフィンまたはそれらの混合物は、ディーゼル燃料に所望の性質にもとづいてディーゼル燃料として使用され得る。フィッシャー−トロプシュ工程からの画分は、代表的に高レベルのn−パラフィンを含む。そして任意に、その画分は生物学的起源の成分またはそこから分離した成分の加工中に同時に異性化されるか、またはそのまま使用され得る。   N-paraffins, iso-paraffins or mixtures thereof prepared from biological raw materials can be used as diesel fuel based on the properties desired for the diesel fuel. The fraction from the Fischer-Tropsch process typically contains high levels of n-paraffins. And optionally, the fraction can be simultaneously isomerized or used as such during the processing of components of biological origin or components separated therefrom.

生物学的成分は、たとえば、少なくとも2つの工程を含む方法により製造され得、そして任意に、対流操作原理(counter-current operation principle)を利用する。この方法の第一の水素脱酸素工程(任意に対流が行われる)において、生物学的原材料の構造は壊れて、酸素、チッ素、リンおよび硫黄を含む化合物ならびにガスとして軽い炭化水素が除去される。その後、オレフィン結合が水素化される。この方法の第二の異性化工程(任意に対流が行われる)において、異性化を行い分岐した炭化水素鎖を得、これによりパラフィンの低温特性を向上させる。   The biological component can be produced, for example, by a method comprising at least two steps and optionally utilizes a counter-current operation principle. In the first hydrodeoxygenation step of this method (optionally convection is performed), the structure of the biological raw material is broken to remove compounds containing oxygen, nitrogen, phosphorus and sulfur and light hydrocarbons as gases. The Thereafter, the olefinic bonds are hydrogenated. In the second isomerization step (optional convection) of this process, isomerization is performed to obtain branched hydrocarbon chains, thereby improving the low temperature properties of the paraffin.

植物油、動物脂質、魚油およびそれらの混合物から選択される脂肪酸および/または脂肪酸エステルを含む植物、動物または魚を起源とする生物学的原材料が供給原料として使用される。   Biological raw materials originating from plants, animals or fish containing fatty acids and / or fatty acid esters selected from vegetable oils, animal lipids, fish oils and mixtures thereof are used as feedstocks.

生物学的起源の高品質の炭化水素成分(とくに、ディーゼル燃料の成分、イソパラフィン性の溶媒およびランプオイルとして有用である)は、高いセタン価(70を超えるのと同じくらいであり得る)を有する生成物として得られる。また、−30℃未満の濁り点は、60を超えるセタン価によりなお達成され得る。この方法は、所望のセタン価および濁り点により調整され得る。   High quality hydrocarbon components of biological origin (especially useful as diesel fuel components, isoparaffinic solvents and lamp oils) have high cetane numbers (can be as high as over 70) Obtained as product. Also, turbidity points below −30 ° C. can still be achieved with cetane numbers above 60. This method can be adjusted depending on the desired cetane number and turbidity point.

本発明のディーゼル燃料組成物の利点としては、RMEなどのFAMEベースの成分を用いる従来技術の溶液と比較して、低温時の優れた性能および優れたセタン価があげられる。低温時の性能に関する問題は、脂肪酸よりも多い炭素数を有する蝋質のn−パラフィンを異性化してイソパラフィンを与えることによって回避することができる。そのようにして得られた生成物の性質は、とくにディーゼル用途に関して優れており、n−パラフィンは代表的には、70を超えるセタン価を有し、イソパラフィンは60を超えるので、ディーゼルプールのセタン価を向上させる効果を有する。これは、明らかにディーゼル成分としての価値を高めるものである。さらに、異性化生成物の濁り点は、所望のレベル、たとえば−30℃以下に調整され得る。これに対して、RMEの濁り点は約0℃、n−パラフィンは+15℃未満である。以下の表1において、異性化生物学的成分、RMEおよび市販のディーゼル燃料の性質を比較する。   Advantages of the diesel fuel composition of the present invention include superior performance at low temperatures and superior cetane number compared to prior art solutions using FAME-based components such as RME. Problems with low temperature performance can be avoided by isomerizing waxy n-paraffins having more carbon atoms than fatty acids to give isoparaffins. The properties of the product thus obtained are excellent, especially for diesel applications, since n-paraffins typically have a cetane number greater than 70 and isoparaffins greater than 60, It has the effect of improving the value. This obviously increases the value as a diesel component. Furthermore, the turbidity point of the isomerized product can be adjusted to a desired level, for example, -30 ° C or lower. In contrast, the turbidity point of RME is about 0 ° C., and n-paraffin is less than + 15 ° C. In Table 1 below, the properties of isomerized biological components, RME and commercial diesel fuel are compared.

Figure 2005538204
Figure 2005538204

本発明のディーゼル燃料組成物を用いた場合、FAME成分を含む生物学的起源の同様の従来の燃料と比較して、エンジンの汚れは顕著に減少し、かつノイズレベルが明らかに低下する。さらに、組成物の濃度が低下する。この組成物は自動車工学または論理のいかなる変更も必要ない。単位容量あたりの高いエネルギー含量はRMEと比較してさらなる利点を示し得る。   When using the diesel fuel composition of the present invention, engine fouling is significantly reduced and the noise level is clearly reduced compared to similar conventional fuels of biological origin containing FAME components. Furthermore, the concentration of the composition decreases. This composition does not require any changes in automotive engineering or logic. The high energy content per unit volume may show further advantages compared to RME.

本発明による生物学的起源のディーゼル燃料組成物の性質は、粗油にもとづく高品質のディーゼル燃料の性質(芳香族化合物が存在せず、かつFAMEと比較して不純物残渣がない)と一致する。   The properties of the diesel fuel composition of biological origin according to the present invention are consistent with those of a high quality diesel fuel based on crude oil (no aromatics present and no impurity residues compared to FAME) .

本発明の燃料組成物によるチッ素酸化物の放出は、類似のFAMEベースの製品よりも低く、さらに粒子の放出は明らかに低く、かつ粒子中の炭素の割合が低い。生物学的起源の燃料組成物の放出における顕著な改善は、環境に非常に重要である。   The emission of nitrogen oxides by the fuel composition of the present invention is lower than similar FAME-based products, and the emission of particles is clearly lower and the percentage of carbon in the particles is low. Significant improvements in the release of fuel compositions of biological origin are very important to the environment.

ここで、本発明を以下の実施例によって例証するが、これは本発明の範囲を限定することを意図しない。   The invention will now be illustrated by the following examples, which are not intended to limit the scope of the invention.

実施例1
以下の表2は、夏のヨーロッパにおいて使用されている従来のディーゼル燃料(EN 590(D1))の放出性を、60容量%の水素化および異性化トール油(TOFA)と40容量%のヨーロッパの夏のディーゼル燃料EN590を含む組成物の放出性と比較する。
Example 1
Table 2 below shows the release of a conventional diesel fuel (EN 590 (D1)) used in summer Europe, with 60 volume% hydrogenated and isomerized tall oil (TOFA) and 40 volume% Europe. Compared to the release of the composition containing the summer diesel fuel EN590.

Figure 2005538204
Figure 2005538204

実施例2
以下の表3は、フィンランドで市販されているディーゼル燃料ベースの高品質リフォーム(reformed)粗油(Fortum Oyjによって製造されたDITC)の放出性を、30容量%の水素化および異性化トール油(TOFA)と70容量%のDITCを含む組成物、または30容量%のトール油メチルエステル(MME)と70容量%のDITCを含む組成物の放出性と比較する。
Example 2
Table 3 below shows the release of diesel fuel-based high quality reformed crude oil (DITC manufactured by Fortum Oyj) commercially available in Finland, with 30 vol% hydrogenated and isomerized tall oil ( TOFA) and a composition containing 70% by volume DITC, or a composition containing 30% by volume tall oil methyl ester (MME) and 70% by volume DITC.

Figure 2005538204
Figure 2005538204

Claims (8)

ディーゼルエンジン用燃料組成物であって、
a)脂肪酸および/または脂肪酸エステルを水素化および分解して、炭化水素(任意に異性化される)を得ることによって、植物および/または動物および/または魚を起源とする生物学的原材料から調製される成分または成分の混合物を0.1〜99容量%;
b)酸素を含む成分を0〜20容量%;
を含み、ここで、成分a)およびb)はエマルジョンとして混合されるか、またはフィッシャー−トロプシュ工程からの粗油および/または画分にもとづくディーゼル成分中に溶解されることを特徴とするディーゼルエンジン用燃料組成物。
A fuel composition for a diesel engine,
a) prepared from biological raw materials originating from plants and / or animals and / or fish by hydrogenating and decomposing fatty acids and / or fatty acid esters to obtain hydrocarbons (optionally isomerized) 0.1 to 99% by volume of the component or mixture of components to be treated;
b) 0 to 20% by volume of oxygen-containing components;
Wherein the components a) and b) are mixed as an emulsion or dissolved in a diesel component based on crude oil and / or fractions from the Fischer-Tropsch process Fuel composition.
前記燃料組成物が、植物および/または動物および/または魚を起源とする生物学的原材料から調製される成分または成分の混合物を0.1〜80容量%含むことを特徴とする請求項1記載の燃料組成物。 2. The fuel composition comprising 0.1 to 80% by volume of a component or mixture of components prepared from biological raw materials originating from plants and / or animals and / or fish. Fuel composition. 前記生物学的原材料から得られる生成物が異性化される請求項1または2記載の燃料組成物。 The fuel composition according to claim 1 or 2, wherein a product obtained from the biological raw material is isomerized. 前記生物学的原材料が、植物油、動物脂質、魚油およびそれらの混合物からなる群から選択される請求項1、2または3記載の燃料組成物。 The fuel composition according to claim 1, 2 or 3, wherein the biological raw material is selected from the group consisting of vegetable oils, animal lipids, fish oils and mixtures thereof. 前記生物学的原材料が、木ベースの脂質もしくは油または他の植物ベースの脂質もしくは油、遺伝子操作による品種改良植物に含まれる脂質、動物ベースの脂質、乳に含まれる脂質、食品工業の再利用した脂質またはそれらの混合物であることを特徴とする請求項1、2、3または4記載の燃料組成物。 The biological raw material is wood-based lipid or oil or other plant-based lipid or oil, lipid contained in genetically modified breeding plants, animal-based lipid, milk-containing lipid, food industry reuse The fuel composition according to claim 1, wherein the fuel composition is a lipid obtained by mixing the mixture or a mixture thereof. 前記生物学的原材料が、ナタネ油、ナタネ油、カノーラ油、トール油、ヒマワリ油、ダイズ油、アサミ油、オリーブ油、アマニ油、カラシ油、パーム油、ピーナッツ油、ヒマシ油、ココナッツ油、ラード、獣脂または魚油であることを特徴とする請求項5記載の燃料組成物。 The biological raw material is rapeseed oil, rapeseed oil, canola oil, tall oil, sunflower oil, soybean oil, assami oil, olive oil, flaxseed oil, mustard oil, palm oil, peanut oil, castor oil, coconut oil, lard, 6. The fuel composition according to claim 5, wherein the fuel composition is tallow or fish oil. 前記酸素を含む成分が、脂肪族アルコール、エーテル、脂肪酸エステル、水、およびそれらを含む混合物からなる群から選択されることを特徴とする請求項1、2、3、4、5または6記載の燃料組成物。 7. The oxygen-containing component is selected from the group consisting of aliphatic alcohols, ethers, fatty acid esters, water, and mixtures containing them. Fuel composition. 前記植物、動物または魚を起源とする生物学的原材料から調製される成分が、脂肪酸および/または脂肪酸エステルを水素化および分解して、炭素数12〜24の生成物としてn−パラフィンを得て、そして、n−パラフィンを異性化して、イソ−パラフィンを得ることによって得られることを特徴とする請求項1、2、3、4、5、6または7記載の燃料組成物。 Components prepared from biological raw materials originating from the plants, animals or fish hydrogenate and decompose fatty acids and / or fatty acid esters to obtain n-paraffins as products having 12 to 24 carbon atoms. The fuel composition according to claim 1, 2, 3, 4, 5, 6 or 7, wherein the fuel composition is obtained by isomerizing n-paraffin to obtain iso-paraffin.
JP2004533535A 2002-09-06 2003-09-04 Diesel fuel composition containing components based on biological raw materials obtained by hydrogenating and decomposing fatty acids Pending JP2005538204A (en)

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Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007308569A (en) * 2006-05-17 2007-11-29 Nippon Oil Corp A-type heavy oil composition
WO2007138776A1 (en) * 2006-05-31 2007-12-06 Nippon Oil Corporation Gas oil composition
WO2008117856A1 (en) 2007-03-28 2008-10-02 Nippon Oil Corporation Gas oil composition
WO2009020056A1 (en) * 2007-08-08 2009-02-12 Nippon Oil Corporation Gas oil composition
JP2009040856A (en) * 2007-08-08 2009-02-26 Nippon Oil Corp Gas oil composition
JP2009040855A (en) * 2007-08-08 2009-02-26 Nippon Oil Corp Gas oil composition
JP2009126935A (en) * 2007-11-22 2009-06-11 Showa Shell Sekiyu Kk Light oil fuel composition
US7914593B2 (en) 2006-03-31 2011-03-29 Nippon Oil Corporation Fuel composition
US8623104B2 (en) 2006-03-31 2014-01-07 Jx Nippon Oil & Energy Corporation Gas oil composition production method
JP2015004066A (en) * 2006-11-15 2015-01-08 エニ、ソシエタ、ペル、アチオニEni S.P.A. Method of producing hydrocarbon fraction from organism-originated mixture

Families Citing this family (37)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1686165A1 (en) * 2005-02-01 2006-08-02 Gibson Chemical Corporation Method for manufacturing bio-diesel oil containing alkane compounds
US8142527B2 (en) 2005-03-21 2012-03-27 Ben-Gurion University Of The Negev Research And Development Authority Production of diesel fuel from vegetable and animal oils
US8022258B2 (en) 2005-07-05 2011-09-20 Neste Oil Oyj Process for the manufacture of diesel range hydrocarbons
KR101102878B1 (en) * 2005-12-12 2012-01-10 네스테 오일 오와이제이 Process for producing a branched hydrocarbon component
FI20055665L (en) * 2005-12-12 2007-06-13 Neste Oil Oyj A process for making a branched hydrocarbon component
EP2022839A4 (en) * 2006-05-17 2013-07-31 Nippon Mitsubishi Oil Corp Gas-oil composition
FI121425B (en) * 2006-06-14 2010-11-15 Neste Oil Oyj Process for the production of base oil
US8067653B2 (en) * 2006-07-14 2011-11-29 The Governors Of The University Of Alberta Methods for producing fuels and solvents
US7897824B2 (en) 2006-08-16 2011-03-01 Energy & Environmental Research Center Foundation Optimal energy pathway to renewable domestic and other fuels
WO2008138861A1 (en) 2007-05-11 2008-11-20 Shell Internationale Research Maatschappij B.V. Fuel composition
US8523959B2 (en) 2007-07-26 2013-09-03 Chevron U.S.A. Inc. Paraffinic biologically-derived distillate fuels with bio-oxygenates for improved lubricity and methods of making same
US8551327B2 (en) * 2007-12-27 2013-10-08 Exxonmobil Research And Engineering Company Staged co-processing of biofeeds for manufacture of diesel range hydrocarbons
US8309783B2 (en) 2008-11-04 2012-11-13 Energy & Environmental Research Center Foundation Process for the conversion of renewable oils to liquid transportation fuels
US8247632B2 (en) 2008-11-04 2012-08-21 Energy & Environmental Research Center Foundation Process for the conversion of renewable oils to liquid transportation fuels
FR2940314B1 (en) * 2008-12-23 2011-11-18 Total Raffinage Marketing GASOLINE FUEL FOR DIESEL ENGINE HAVING HIGH CARBON CONTENT OF RENEWABLE ORIGIN AND OXYGEN
US8785701B2 (en) * 2008-12-24 2014-07-22 Exxonmobil Research And Engineering Company Co-processing of diesel biofeed and kerosene range hydrocarbons
US8632675B2 (en) 2008-12-24 2014-01-21 Exxonmobil Research And Engineering Company Co-processing of diesel biofeed and heavy oil
CN102481555B (en) 2009-06-12 2015-10-07 阿尔比马尔欧洲有限公司 SAPO molecular sieve catalyst and preparation thereof and purposes
HU231091B1 (en) 2009-09-30 2020-07-28 Mol Magyar Olaj- És Gázipari Nyilvánosan Működő Részvénytársaság Fuels and fuel additives for combustion engines and method for producing them
IT1396939B1 (en) 2009-12-09 2012-12-20 Eni Spa USEFUL HYDROCARBURIC COMPOSITION AS FUEL OR FUEL
US8853474B2 (en) 2009-12-29 2014-10-07 Exxonmobil Research And Engineering Company Hydroprocessing of biocomponent feedstocks with low purity hydrogen-containing streams
FI125632B (en) 2010-05-25 2015-12-31 Upm Kymmene Corp Method and apparatus for producing hydrocarbons
EP2514803B1 (en) 2011-04-21 2017-02-01 Infineum International Limited Improvements in fuel oils
RU2466180C1 (en) * 2011-08-09 2012-11-10 Закрытое акционерное общество "Центральный ордена Трудового Красного Знамени научно-исследовательский и проектно-конструкторский институт морского флота" Masout additive
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US8884086B2 (en) 2011-09-14 2014-11-11 Bp Corporation North America Inc. Renewable diesel refinery strategy
RU2544239C2 (en) * 2012-11-19 2015-03-20 Общество с ограниченной ответственностью "РЕЦИКЛ" Biofuel composition
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FI127307B (en) * 2017-01-27 2018-03-15 Neste Oyj Refined fuel compositions and methods for their preparation
CN110382669A (en) * 2017-02-21 2019-10-25 埃克森美孚研究工程公司 Diesel boiling range fuels blend and its manufacturing method
FI130601B (en) 2018-12-14 2023-12-07 Neste Oyj Diesel fuel composition
CN110499178A (en) * 2019-08-27 2019-11-26 易高生物化工科技(张家港)有限公司 A kind of method that waste animal and vegetable oil adds hydrogen to prepare atoleine
FR3119625B1 (en) * 2021-07-02 2023-02-17 Totalenergies Marketing Services Composition of fuel rich in aromatic compounds, paraffins and ether, and its use in motor vehicles
BR102021016123A2 (en) * 2021-08-16 2023-02-23 Petróleo Brasileiro S.A. - Petrobras PROCESS FOR BIODIESEL PRODUCTION FROM ACID CARDS
US11851624B2 (en) * 2021-10-20 2023-12-26 Shell Usa, Inc. Biofuel blends with improved oxidation stability and lubricity

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002501570A (en) * 1997-05-29 2002-01-15 フォアタム オイル アンド ガス オサケ ユキテュア Manufacturing process of high-grade diesel fuel

Family Cites Families (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4992605A (en) * 1988-02-16 1991-02-12 Craig Wayne K Production of hydrocarbons with a relatively high cetane rating
CA2149685C (en) * 1994-06-30 1999-09-14 Jacques Monnier Conversion of depitched tall oil to diesel fuel additive
FI100248B (en) * 1996-02-05 1997-10-31 Fortum Oil Oy Manufacture of middle distillate
US5814109A (en) * 1997-02-07 1998-09-29 Exxon Research And Engineering Company Diesel additive for improving cetane, lubricity, and stability
US6458265B1 (en) * 1999-12-29 2002-10-01 Chevrontexaco Corporation Diesel fuel having a very high iso-paraffin to normal paraffin mole ratio
US6787022B1 (en) * 2000-05-02 2004-09-07 Exxonmobil Research And Engineering Company Winter diesel fuel production from a fischer-tropsch wax
CA2406287C (en) * 2000-05-02 2010-04-06 Exxonmobil Research And Engineering Company Wide cut fischer-tropsch diesel fuels

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002501570A (en) * 1997-05-29 2002-01-15 フォアタム オイル アンド ガス オサケ ユキテュア Manufacturing process of high-grade diesel fuel

Cited By (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8623103B2 (en) 2006-03-31 2014-01-07 Jx Nippon Oil & Energy Corporation Method for producing gas oil composition
US8628592B2 (en) 2006-03-31 2014-01-14 Jx Nippon Oil & Energy Corporation Method for producing gas oil composition
US7914593B2 (en) 2006-03-31 2011-03-29 Nippon Oil Corporation Fuel composition
US8623104B2 (en) 2006-03-31 2014-01-07 Jx Nippon Oil & Energy Corporation Gas oil composition production method
JP2007308569A (en) * 2006-05-17 2007-11-29 Nippon Oil Corp A-type heavy oil composition
WO2007138776A1 (en) * 2006-05-31 2007-12-06 Nippon Oil Corporation Gas oil composition
US8795394B2 (en) 2006-05-31 2014-08-05 Nippon Oil Corporation Gas oil composition
JP2015004066A (en) * 2006-11-15 2015-01-08 エニ、ソシエタ、ペル、アチオニEni S.P.A. Method of producing hydrocarbon fraction from organism-originated mixture
WO2008117856A1 (en) 2007-03-28 2008-10-02 Nippon Oil Corporation Gas oil composition
WO2009020056A1 (en) * 2007-08-08 2009-02-12 Nippon Oil Corporation Gas oil composition
JP2009040855A (en) * 2007-08-08 2009-02-26 Nippon Oil Corp Gas oil composition
JP2009040856A (en) * 2007-08-08 2009-02-26 Nippon Oil Corp Gas oil composition
JP2009126935A (en) * 2007-11-22 2009-06-11 Showa Shell Sekiyu Kk Light oil fuel composition

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