JP4482469B2 - Method for producing light oil composition - Google Patents
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本発明は、軽油組成物、特にディーゼル自動車用の燃料油に用いる軽油組成物に関し、詳しくは、酸化安定性に優れる低硫黄軽油組成物に関する。 The present invention relates to a light oil composition, particularly a light oil composition used for a fuel oil for diesel automobiles, and more particularly to a low sulfur light oil composition having excellent oxidation stability.
ディーゼル車から排出されるＮＯｘや粒子状物質を低減することは社会的要請であり、ディーゼル車用燃料油に用いる軽油には、粒子状物質の一成分であるサルフェートを低減し、かつ排出ガスの後処理装置における触媒被毒を抑制し、後処理効率を向上させるために、低硫黄化することが求められている。軽油の低硫黄化の手段としては、軽油留分を水素化脱硫処理することが一般的に挙げられるが、水素化脱硫においては、軽油留分中の硫黄分のみならず、軽油留分中に元々含有されている抗酸化性物質（例えば、アミン類、フェノール類等）も水素化処理される場合もあり、水素化脱硫の進んだ低硫黄軽油では、酸化安定性に劣り、過酸化物が生成する場合があることが知られている（例えば、非特許文献１、非特許文献２参照）。 It is a social requirement to reduce NOx and particulate matter emitted from diesel vehicles. In diesel oil used in diesel vehicle fuel oil, the sulfate, which is a component of particulate matter, is reduced, and the exhaust gas In order to suppress catalyst poisoning in the aftertreatment device and improve the aftertreatment efficiency, it is required to reduce the sulfur content. As a means for reducing the sulfur content of diesel oil, hydrodesulfurization treatment of diesel oil fractions is generally cited. In hydrodesulphurization, not only sulfur content in diesel oil fractions but also diesel oil fractions are used. Antioxidant substances (eg, amines, phenols, etc.) originally contained may be hydrotreated, and low sulfur gas oils that have undergone hydrodesulfurization are inferior in oxidative stability and have peroxides. It is known that it may be generated (see, for example, Non-Patent Document 1 and Non-Patent Document 2).
また、軽油の酸化安定性は、重要な実用性能の一つであり、軽油において、特に酸化安定性の低下した低硫黄化軽油において、過酸化物の生成などを抑制することは重要な課題である。酸化安定性の向上には、酸化防止剤を添加することが有効であるが、酸化防止剤を添加することは経済的に不利である（例えば、非特許文献３参照）。 In addition, the oxidation stability of light oil is one of the important practical performances. In light oil, especially in low-sulfurized light oil with reduced oxidation stability, it is an important issue to suppress the formation of peroxides. is there. In order to improve the oxidation stability, it is effective to add an antioxidant, but it is economically disadvantageous to add an antioxidant (for example, see Non-Patent Document 3).
本発明は、このような状況下で、酸化防止剤を添加することなしに、酸化安定性に優れた低硫黄軽油組成物を提供することを目的とするものである。 An object of the present invention is to provide a low-sulfur gas oil composition excellent in oxidation stability without adding an antioxidant under such circumstances.
本発明者らは、低硫黄軽油の酸化安定性について鋭意検討した結果、ナフテンベンゼン類とフルオレン類の含有量、及びナフタレン類の含有量が一定範囲である場合に酸化安定性に優れることを見出し、本発明を完成するに至った。 As a result of intensive studies on the oxidation stability of low-sulfur gas oil, the present inventors have found that the content of naphthenebenzenes and fluorenes and that the content of naphthalenes is in a certain range are excellent in oxidation stability. The present invention has been completed.
すなわち、本発明は、上記目的を達成するために、次の軽油組成物の製造方法を提供するものである。
（１）ナフテンベンゼン類およびフルオレン類を含み、沸点範囲１８２〜３６７℃の直留軽油留分を、硫黄分が１０質量ｐｐｍ以下、ナフテンベンゼン類とフルオレン類の含有量の和が５．６２容量％以下となるように水素化脱硫して得た脱硫軽油と、
ナフテンベンゼン類およびフルオレン類を含み、沸点範囲１４８〜２７１℃の直留灯油を、硫黄分が１０質量ｐｐｍ以下、ナフテンベンゼン類とフルオレン類の含有量の和が３．８４容量％以下となるように水素化脱硫して得た脱硫灯油とを混合し、
硫黄分の含有量が１０質量ｐｐｍ以下であり、ナフテンベンゼン類とフルオレン類の含有量の和が８．０容量％以下であり、ナフタレン類の含有量が０．５容量％以上３．０容量％以下である軽油組成物を調製することを特徴とする、酸化安定性に優れた軽油組成物の製造方法。
（２）前記脱硫軽油を８０容量％、前記脱硫灯油を２０容量％配合したことを特徴とする、上記（１）に記載の軽油組成物の製造方法。
That is, this invention provides the manufacturing method of the following light oil composition, in order to achieve the said objective.
(1) A straight-run gas oil fraction containing naphthenebenzenes and fluorenes and having a boiling range of 182 to 367 ° C., a sulfur content of 10 mass ppm or less, and the sum of the contents of naphthenebenzenes and fluorenes is 5.62 volumes % Desulfurized diesel oil obtained by hydrodesulfurization to be less than
A straight-run kerosene containing naphthenebenzenes and fluorenes and having a boiling point range of 148 to 271 ° C. so that the sulfur content is 10 mass ppm or less and the sum of the contents of naphthenebenzenes and fluorenes is 3.84 vol% or less. Is mixed with desulfurized kerosene obtained by hydrodesulfurization,
The sulfur content is 10 ppm by mass or less, the total content of naphthenebenzenes and fluorenes is 8.0% by volume or less, and the content of naphthalenes is 0.5% by volume to 3.0% by volume. % Or less, a method for producing a light oil composition excellent in oxidative stability, characterized by comprising preparing a light oil composition that is not more than%.
(2) The method for producing a light oil composition according to the above (1) , wherein 80% by volume of the desulfurized gas oil and 20% by volume of the desulfurized kerosene are blended .
本発明によれば、酸化防止剤を添加することなしに、酸化安定性に優れた低硫黄軽油組成物を提供することができる。 According to the present invention, it is possible to provide a low sulfur gas oil composition having excellent oxidation stability without adding an antioxidant.
以下、本発明の内容を更に詳しく説明する。
本発明の軽油組成物において、硫黄分の含有量は５０質量ｐｐｍ以下であり、好ましくは１０質量ｐｐｍ以下である。硫黄分の含有量が５０質量ｐｐｍ以下であれば、ディーゼルエンジンから排出される粒子状物質の成分であるサルフェートの排出量が少なくなり、更に排ガス後処理装置の性能に悪影響を及ぼすことなく、なお更にはその他の好ましからざる排出ガス成分の増加が抑制される。硫黄分の含有量は、ＪＩＳ Ｋ ２５４１の微量電量滴定式酸化法により測定できる。
Hereinafter, the contents of the present invention will be described in more detail.
In the light oil composition of the present invention, the sulfur content is 50 ppm by mass or less, preferably 10 ppm by mass or less. If the sulfur content is 50 ppm by mass or less, the amount of sulfate that is a component of the particulate matter discharged from the diesel engine is reduced, and further, the performance of the exhaust gas aftertreatment device is not adversely affected. Furthermore, an increase in other undesirable exhaust gas components is suppressed. The sulfur content can be measured by a microcoulometric titration method according to JIS K2541.
本発明の軽油組成物においては、ナフテンベンゼン類とフルオレン類の含有量の和が８．０容量％以下であり、好ましくは７．５容量％以下、更に好ましくは７．０容量％以下である。ナフテンベンゼン類とフルオレン類の含有量の和が８．０容量％以下であれば、酸化安定性に優れ、長期保存中に過酸化物などが生成することもない。
ナフテンベンゼン類とは、テトラリン、アルキル基置換テトラリン、インダン、アルキル基置換インダンなどを示す。また、フルオレン類とは、フルオレン、アルキル基置換フルオレンなどを示す。
In the light oil composition of the present invention, the total content of naphthenebenzenes and fluorenes is 8.0% by volume or less, preferably 7.5% by volume or less, and more preferably 7.0% by volume or less. . When the sum of the contents of naphthenebenzenes and fluorenes is 8.0% by volume or less, the oxidation stability is excellent and peroxides are not generated during long-term storage.
The naphthenebenzenes include tetralin, alkyl group-substituted tetralin, indane, alkyl group-substituted indane and the like. The fluorenes include fluorene, alkyl group-substituted fluorene and the like.
また、本発明の軽油組成物においては、ナフタレン類の含有量が０．５容量％以上３．０容量％以下であり、好ましくは０．６容量％以上３．０容量％以下である。ナフタレン類の含有量がこの範囲にあれば、酸化安定性に優れ、かつ長期保存中に過酸化物などが生成することもなく、また、ディーゼルエンジンから排出される粒子状物質が少なくなる。 ナフタレン類とは、ナフタレン、アルキル基置換ナフタレンなどを示す。 Moreover, in the light oil composition of this invention, content of naphthalene is 0.5 volume% or more and 3.0 volume% or less, Preferably it is 0.6 volume% or more and 3.0 volume% or less. If the content of naphthalene is in this range, the oxidation stability is excellent, peroxides are not generated during long-term storage, and particulate matter discharged from the diesel engine is reduced. Naphthalene refers to naphthalene, alkyl group-substituted naphthalene, and the like.
本発明の実施に当たり、ナフテンベンゼン類、フルオレン類、ナフタレン類の含有量は以下の方法により測定できる。すなわち、まず、高速液体クロマトグラフ（ＨＰＬＣ）により軽油組成物を芳香族分と飽和分に分画して各分画物を採取した後、その各分画物を、ガスクロマトグラフ装置（ＧＣ）と質量分析装置（ＭＳ）を複合したガスクロマトグラフ質量分析装置（ＧＣ−ＭＳ）で測定し、飽和分はＡＳＴＭ Ｄ ２７８６に従って、芳香族分はＡＳＴＭ Ｄ ３２３９に従って解析を行い、各分画物中のタイプ別組成割合を容量％で算出する。次に、軽油組成物中に占める各分画物の割合を、ＪＰＩ−５Ｓ−４９−９７「石油製品−炭化水素タイプ試験方法−高速液体クロマトグラフ法」に基づいて求め、各分画物の割合に、ＧＣ−ＭＳで求めた分画物中のタイプ別組成割合を乗じて、軽油組成物中のナフテンベンゼン類、フルオレン類、ナフタレン類の含有量を求める。 In carrying out the present invention, the content of naphthenebenzenes, fluorenes, and naphthalenes can be measured by the following method. That is, first, a gas oil composition was fractionated into an aromatic component and a saturated component by high performance liquid chromatography (HPLC), and each fraction was collected. Then, each fraction was separated from a gas chromatograph (GC). Measured with a gas chromatograph mass spectrometer (GC-MS) combined with a mass spectrometer (MS). Saturates are analyzed according to ASTM D 2786, aromatics are analyzed according to ASTM D 3239, and the type in each fraction Another composition ratio is calculated by volume%. Next, the ratio of each fraction in the light oil composition was determined based on JPI-5S-49-97 “Petroleum products—Hydrocarbon type test method—High performance liquid chromatograph method”. The content of naphthenebenzenes, fluorenes, and naphthalenes in the light oil composition is determined by multiplying the ratio by the composition ratio by type in the fraction obtained by GC-MS.
本発明の軽油組成物は、最終的に得られる軽油組成物が上記に規定する特定の性状を有するように、一種又は二種以上の軽油基材を混合して調製できる。
本発明の軽油組成物の調製に用いる軽油基材としては、最終的に得られる軽油組成物が上記に規定する特定の性状を有する限りにおいて、種々の軽油基材を適宜用いることができる。例えば、原油を常圧蒸留して得られる灯油留分や軽油留分、及びそれらを脱硫した脱硫灯油や脱硫軽油を用いることができる。また、直接脱硫装置から得られる直接脱硫軽油、間接脱硫装置から得られる間接脱硫軽油、流動接触分解装置から得られる軽質サイクルオイル、及びそれらを常圧蒸留装置から得られる軽油留分と混合して更に脱硫処理した基材などを用いることができて、通常軽油組成物の基材として使用されるものを適宜用いることができる。その他に、フィッシャートロプシュ合成およびそれに付随する各種二次処理プロセスにより得られる各種炭化水素の軽油相当留分や含酸素化合物などを基材として用いることもできる。また、最終的に得られる軽油組成物が上記に規定する特定の性状を有するようにすることは、用いる軽油基材の硫黄分、ナフテンベンゼン類、フルオレン類、ナフタレン類の各含有量を考慮してその配合割合を選択することによって達成し得る。中でも、脱硫灯油や脱硫軽油を基材として用いることにより本発明の軽油組成物を好適に調製することができる。
The light oil composition of the present invention can be prepared by mixing one or two or more light oil base materials so that the finally obtained light oil composition has the specific properties defined above.
As the light oil base material used for the preparation of the light oil composition of the present invention, various light oil base materials can be appropriately used as long as the finally obtained light oil composition has the specific properties defined above. For example, a kerosene fraction or a light oil fraction obtained by atmospheric distillation of crude oil, and a desulfurized kerosene or a desulfurized gas oil obtained by desulfurizing them can be used. In addition, the direct desulfurization gas oil obtained from the direct desulfurization device, the indirect desulfurization gas oil obtained from the indirect desulfurization device, the light cycle oil obtained from the fluid catalytic cracking device, and the light oil fraction obtained from the atmospheric distillation device are further mixed. A desulfurized base material or the like can be used, and those normally used as a base material for a light oil composition can be appropriately used. In addition, various hydrocarbon light oil equivalent fractions and oxygen-containing compounds obtained by Fischer-Tropsch synthesis and various secondary treatment processes associated therewith can be used as a base material. In addition, the final light oil composition should have the specific properties specified above in consideration of the sulfur content, naphthenebenzenes, fluorenes, and naphthalenes of the light oil base used. This can be achieved by selecting the blending ratio. Among these, the light oil composition of the present invention can be suitably prepared by using desulfurized kerosene or desulfurized light oil as a base material.
また、本発明の軽油組成物には、必要に応じて各種の添加剤を適宜配合することができる。このような添加剤としては、セタン価向上剤、界面活性剤、流動性向上剤、防腐剤、防錆剤、泡消剤、清浄剤、色相改善剤、潤滑性向上剤など公知の燃料添加剤が挙げられる。これらを一種又は二種以上組み合わせて添加することができる。
また、本発明は、酸化防止剤を添加することなしに、酸化安定性に優れた低硫黄軽油組成物を提供するものであるが、本発明に酸化防止剤を添加した場合は更に酸化安定性を向上させることが可能となる。
Moreover, various additives can be suitably mix | blended with the light oil composition of this invention as needed. Examples of such additives include known fuel additives such as cetane number improvers, surfactants, fluidity improvers, antiseptics, rust inhibitors, defoamers, detergents, hue improvers, and lubricity improvers. Is mentioned. These can be added singly or in combination of two or more.
In addition, the present invention provides a low sulfur gas oil composition excellent in oxidation stability without adding an antioxidant. However, when an antioxidant is added to the present invention, the oxidation stability is further increased. Can be improved.
以下に本発明の内容を実験例及び比較例により更に詳しく説明するが、本発明はこれらによって制限されるものではない。 Hereinafter, the contents of the present invention will be described in more detail with reference to experimental examples and comparative examples, but the present invention is not limited thereto.
ここでは、表１に示すような基材を用いて各軽油組成物を調製した。さらに各基材の性状を表２に示した。 Here, each light oil composition was prepared using a base material as shown in Table 1. Further, the properties of each substrate are shown in Table 2.
実施例１
沸点範囲１８２℃〜３６７℃の直留軽油留分を硫黄分１０質量ｐｐｍ以下に脱硫処理した脱硫軽油（基材１）８０容量％と沸点範囲１４８℃〜２７１℃の直留灯油を硫黄分１０質量ｐｐｍ以下に脱硫処理した脱硫灯油（基材２）を２０容量％の割合で混合し、表４に示す性状の軽油組成物を得た。
Example 1
80% by volume of desulfurized gas oil (base material 1) obtained by desulfurizing a straight-run gas oil fraction having a boiling range of 182 ° C. to 367 ° C. to a sulfur content of 10 mass ppm or less and straight-run kerosene having a boiling range of 148 ° C. to 271 ° C. having a sulfur content of 10 Desulfurized kerosene (base material 2) desulfurized to mass ppm or less was mixed at a rate of 20% by volume to obtain light oil compositions having the properties shown in Table 4.
参考例２
常圧蒸留装置から留出する直留軽油留分に流動接触分解装置から留出する軽質サイクルオイルを６容量％配合し沸点範囲１９３℃〜３６８℃とした軽油留分を、硫黄分２０質量ｐｐｍ以下に脱硫処理し（基材３）、表４に示す軽油組成物を得た。
Reference Example 2
A gas oil fraction having a boiling point range of 193 ° C. to 368 ° C. by blending 6% by volume of light cycle oil distilled from a fluid catalytic cracking device with a straight-run gas oil fraction distilled from an atmospheric distillation unit, and having a sulfur content of 20 mass ppm or less The gas oil composition shown in Table 4 was obtained.
比較例１
基材１を１９．８容量％と基材２を７９．２容量％に、フルオレンを１．０容量％添加し、表４に示す性状の軽油組成物を得た。
比較例２
常圧蒸留装置から留出する直留軽油留分に流動接触分解装置から留出する軽質サイクルオイルを６容量％配合し沸点範囲１９３℃〜３６８℃とした軽油留分を、硫黄分５０質量ｐｐｍ以下に脱硫処理し（基材４）、表４に示す軽油組成物を得た。
Comparative Example 1
Base oil 1 was added to 19.8% by volume, base material 2 was added to 79.2% by volume, and fluorene was added to 1.0% by volume to obtain a light oil composition having the properties shown in Table 4.
Comparative Example 2
A gas oil fraction having a boiling point range of 193 ° C. to 368 ° C. by blending 6% by volume of light cycle oil distilled from a fluid catalytic cracking device with a straight-run gas oil fraction distilled from an atmospheric distillation unit, and having a sulfur content of 50 mass ppm or less (4) to obtain a light oil composition shown in Table 4.
上記のように調製した、各軽油組成物の配合割合を表３にまとめた。 Table 3 summarizes the blending ratio of each light oil composition prepared as described above.
実施例１、参考例２および比較例１、２の各軽油組成物について、硫黄分を微量電量滴定式酸化法により測定した。軽油組成物中に占めるナフテンベンゼン類、フルオレン類、ナフタレン類は、以下に示した装置、条件により測定した。 About each light oil composition of Example 1, Reference Example 2, and Comparative Examples 1 and 2, the sulfur content was measured by a microcoulometric titration oxidation method. The naphthenebenzenes, fluorenes, and naphthalenes in the light oil composition were measured by the following apparatus and conditions.
飽和分と芳香族分の割合：
Agilent 1100 Series（ALS:G1329A, Bin Pump: G1312A, Degasser: G1379A, Rid: G1362A, Colcom: G1316A）により、移動相：n−ヘキサン、流量1.0ml/min、カラム：硝酸銀含浸シリカカラム（4.6mml.D.*70mmL. センシュー科学製 AgNO3-1071-Y）、アミン修飾カラム（4.0mml.D.*250mmL. ２本 センシュー科学製 LICHROSORB-NH2）、カラム温度：35℃、試料濃度：10vol.%、注入量5μlの条件で測定した。
Saturation and aromatic content:
According to Agilent 1100 Series (ALS: G1329A, Bin Pump: G1312A, Degasser: G1379A, Rid: G1362A, Colcom: G1316A), mobile phase: n-hexane, flow rate 1.0 ml / min, column: silver nitrate impregnated silica column (4.6 mml. D. * 70mmL. Senshu Scientific AgNO3-1071-Y), amine modified column (4.0mml.D. * 250mmL. 2 Senshu Scientific LICHROSORB-NH2), column temperature: 35 ° C, sample concentration: 10vol.%, The measurement was performed under an injection volume of 5 μl.
芳香族分中のタイプ別組成割合：
試料をHPLCにより飽和分と芳香族分により分画後、芳香族分について、ＨＰ−６８９０シリーズII ＨＰ５９７３ 四重極質量分析計により、
カラム：DＢ−１：３０ｍ×０．２５ｍｍＩ．Ｄ．×０．２５ｕｍ、
オーブン温度：４０℃（１ｍｉｎ）→１０℃／ｍｉｎ→２８０℃（５ｍｉｎ）、
注入口温度：４３℃ Ｏｖｅｎ track mode ON、
インターフェース温度：３００℃、
キャリアーガス：Ｈｅ：５５ＫＰａ Constant flow mode ＯＮ、
Ｓｏｌｖｅｎｔ Ｄｅｌａｙ：４．５ｍｉｎ、
質量範囲：５０〜５００ Ｔｈｒｅｓｈｏｌｄ＝１００ Ｓａｍｐｌｉｎｇ♯３、
イオン化電圧：７０ｅＶ、
注入方法：オンカラム注入 ３．０ｕｌ、
メソッドファイル：ＴＹＰＥ−ＡＮＡ．Ｍ（芳香族分）、
の条件で測定し、芳香族分中に占めるナフテンベンゼン類、フルオレン類、ナフタレン類の割合を求めた。
Composition ratio by type in aromatics:
After the sample was fractionated by saturated and aromatic components by HPLC, the aromatic content was analyzed by HP-6890 Series II HP5973 quadrupole mass spectrometer.
Column: DB-1: 30 m × 0.25 mm I.D. D. × 0.25um,
Oven temperature: 40 ° C. (1 min) → 10 ° C./min→280° C. (5 min),
Inlet temperature: 43 ° C. Even track mode ON,
Interface temperature: 300 ° C
Carrier gas: He: 55 KPa Constant flow mode ON,
Solvent Delay: 4.5 min.
Mass range: 50-500 Threshold = 100 Sampling # 3,
Ionization voltage: 70 eV,
Injection method: On-column injection 3.0ul,
Method file: TYPE-ANA. M (aromatic component),
The ratio of naphthenebenzenes, fluorenes, and naphthalenes in the aromatic content was determined.
軽油組成物中のナフテンベンゼン類、フルオレン類、ナフタレン類の含有量：
軽油組成物中に占める芳香族分の割合に、芳香族分中のタイプ別組成割合を乗じて、軽油組成物中のナフテンベンゼン類、フルオレン類、ナフタレン類の含有量を求めた。
Content of naphthenebenzenes, fluorenes, naphthalenes in light oil composition:
The content of naphthenebenzenes, fluorenes, and naphthalenes in the light oil composition was determined by multiplying the ratio of the aromatic content in the light oil composition by the composition ratio by type in the aromatic content.
実施例１、参考例２および比較例１、２の各軽油組成物について、ＪＩＳ Ｋ ２２８７に記載のガソリン酸化安定度試験装置を用いて、軽油組成物５０ｍｌに対して酢酸銅（０．２０ｍｇＣｕ／ｍｌ）を２ｍｌ添加したサンプルをボンベに入れ、酸素を６８９〜７０３ｋＰａまで圧入し１００℃で４８時間貯蔵した。ボンベの圧力変化を測定し、４８時間後の圧力降下値を測定した。圧力降下値は貯蔵中に消費された酸素量を示しており、この値が大きいほど酸素がサンプルと反応したことになり、すなわち酸化安定性に劣ることを示す。また、酸化安定性は、軽油組成物に含有する硫黄分、ナフテンベンゼン類、フルオレン類、ナフタレン類と密接な関係がある。特に過酸化物の生成原因となりやすいナフテンベンゼン類とフルオレン類の含有量を本発明のように規定した場合、圧力降下値が５．４×１００ｋＰａ以上になると長期貯蔵中に過酸化物が生成する傾向が強くなることを確認しており、酸化安定性に優れる軽油組成物を提供するためには、圧力降下値は５．４×１００ｋＰａ以下であることが好ましい。
結果を表４に示す。
About each light oil composition of Example 1, Reference Example 2, and Comparative Examples 1 and 2, using a gasoline oxidation stability test apparatus described in JIS K 2287, copper acetate (0.20 mgCu / ml) was added to a cylinder, and oxygen was injected to 689 to 703 kPa and stored at 100 ° C. for 48 hours. The pressure change of the cylinder was measured, and the pressure drop value after 48 hours was measured. The pressure drop value indicates the amount of oxygen consumed during storage, and the larger the value, the more the oxygen has reacted with the sample, that is, the lower the oxidation stability. Further, the oxidation stability is closely related to the sulfur content, naphthenebenzenes, fluorenes, and naphthalenes contained in the light oil composition. In particular, when the contents of naphthenebenzenes and fluorenes, which are likely to cause peroxides, are specified as in the present invention, peroxides are generated during long-term storage when the pressure drop value is 5.4 × 100 kPa or more. The pressure drop value is preferably 5.4 × 100 kPa or less in order to provide a light oil composition that has been confirmed to have a strong tendency and has excellent oxidation stability.
The results are shown in Table 4.
表４に示す結果から、本発明の範囲外である比較例１、２の軽油組成物は高い圧力降下値を示しているのに対し、本発明の実施例１の軽油組成物は低い圧力降下値を示しており、酸化安定性に優れていることが分かる。 From the results shown in Table 4, the light oil compositions of Comparative Examples 1 and 2 that are outside the scope of the present invention show high pressure drop values, whereas the light oil composition of Example 1 of the present invention has a low pressure drop. It shows that the value is excellent and the oxidation stability is excellent.
Claims (2)
ナフテンベンゼン類およびフルオレン類を含み、沸点範囲１４８〜２７１℃の直留灯油を、硫黄分が１０質量ｐｐｍ以下、ナフテンベンゼン類とフルオレン類の含有量の和が３．８４容量％以下となるように水素化脱硫して得た脱硫灯油とを混合し、
硫黄分の含有量が１０質量ｐｐｍ以下であり、ナフテンベンゼン類とフルオレン類の含有量の和が８．０容量％以下であり、ナフタレン類の含有量が０．５容量％以上３．０容量％以下である軽油組成物を調製することを特徴とする、酸化安定性に優れた軽油組成物の製造方法。 A straight-run gas oil fraction containing naphthenebenzenes and fluorenes and having a boiling point range of 182 to 367 ° C. has a sulfur content of 10 mass ppm or less, and the total content of naphthenebenzenes and fluorenes is 5.62% by volume or less. Desulfurized gas oil obtained by hydrodesulfurization so that
A straight-run kerosene containing naphthenebenzenes and fluorenes and having a boiling point range of 148 to 271 ° C. so that the sulfur content is 10 mass ppm or less and the sum of the contents of naphthenebenzenes and fluorenes is 3.84 vol% or less. Is mixed with desulfurized kerosene obtained by hydrodesulfurization,
The sulfur content is 10 ppm by mass or less, the total content of naphthenebenzenes and fluorenes is 8.0% by volume or less, and the content of naphthalenes is 0.5% by volume to 3.0% by volume. % Or less, a method for producing a light oil composition excellent in oxidative stability, characterized by comprising preparing a light oil composition that is not more than%.
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| US10494579B2 (en) | 2016-04-26 | 2019-12-03 | Exxonmobil Research And Engineering Company | Naphthene-containing distillate stream compositions and uses thereof |
| US10550335B2 (en) | 2015-12-28 | 2020-02-04 | Exxonmobil Research And Engineering Company | Fluxed deasphalter rock fuel oil blend component oils |
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| JP5730006B2 (en) | 2010-12-24 | 2015-06-03 | 昭和シェル石油株式会社 | Light oil composition |
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| US10550335B2 (en) | 2015-12-28 | 2020-02-04 | Exxonmobil Research And Engineering Company | Fluxed deasphalter rock fuel oil blend component oils |
| US10550341B2 (en) | 2015-12-28 | 2020-02-04 | Exxonmobil Research And Engineering Company | Sequential deasphalting for base stock production |
| US10590360B2 (en) | 2015-12-28 | 2020-03-17 | Exxonmobil Research And Engineering Company | Bright stock production from deasphalted oil |
| US10647925B2 (en) | 2015-12-28 | 2020-05-12 | Exxonmobil Research And Engineering Company | Fuel components from hydroprocessed deasphalted oils |
| US10808185B2 (en) | 2015-12-28 | 2020-10-20 | Exxonmobil Research And Engineering Company | Bright stock production from low severity resid deasphalting |
| US10947464B2 (en) | 2015-12-28 | 2021-03-16 | Exxonmobil Research And Engineering Company | Integrated resid deasphalting and gasification |
| US10494579B2 (en) | 2016-04-26 | 2019-12-03 | Exxonmobil Research And Engineering Company | Naphthene-containing distillate stream compositions and uses thereof |
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