Classifications

• • C—CHEMISTRY; METALLURGY
  • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
  • C10L—FUELS 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
  • C10L1/00—Liquid carbonaceous fuels
  • C10L1/04—Liquid carbonaceous fuels essentially based on blends of hydrocarbons
• • C—CHEMISTRY; METALLURGY
  • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
  • C10L—FUELS 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
  • C10L10/00—Use of additives to fuels or fires for particular purposes
  • C10L10/14—Use of additives to fuels or fires for particular purposes for improving low temperature properties
  • C10L10/16—Pour-point depressants
• • C—CHEMISTRY; METALLURGY
  • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
  • C10L—FUELS 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
  • C10L1/00—Liquid carbonaceous fuels
  • C10L1/10—Liquid carbonaceous fuels containing additives
  • C10L1/14—Organic compounds
  • C10L1/18—Organic compounds containing oxygen
  • C10L1/192—Macromolecular compounds
  • C10L1/195—Macromolecular compounds obtained by reactions involving only carbon-to-carbon unsaturated bonds
  • C10L1/196—Macromolecular compounds obtained by reactions involving only carbon-to-carbon unsaturated bonds derived from monomers containing a carbon-to-carbon unsaturated bond and a carboxyl group or salts, anhydrides or esters thereof homo- or copolymers of compounds having one or more unsaturated aliphatic radicals each having one carbon bond to carbon double bond, and at least one being terminated by a carboxyl radical or of salts, anhydrides or esters thereof
  • C10L1/1963—Macromolecular compounds obtained by reactions involving only carbon-to-carbon unsaturated bonds derived from monomers containing a carbon-to-carbon unsaturated bond and a carboxyl group or salts, anhydrides or esters thereof homo- or copolymers of compounds having one or more unsaturated aliphatic radicals each having one carbon bond to carbon double bond, and at least one being terminated by a carboxyl radical or of salts, anhydrides or esters thereof mono-carboxylic
• • C—CHEMISTRY; METALLURGY
  • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
  • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
  • C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
  • C10G2300/10—Feedstock materials
  • C10G2300/1022—Fischer-Tropsch products
• • C—CHEMISTRY; METALLURGY
  • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
  • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
  • C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
  • C10G2300/20—Characteristics of the feedstock or the products
  • C10G2300/201—Impurities
  • C10G2300/202—Heteroatoms content, i.e. S, N, O, P
• • C—CHEMISTRY; METALLURGY
  • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
  • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
  • C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
  • C10G2300/20—Characteristics of the feedstock or the products
  • C10G2300/30—Physical properties of feedstocks or products
  • C10G2300/302—Viscosity
• • C—CHEMISTRY; METALLURGY
  • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
  • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
  • C10G2400/00—Products obtained by processes covered by groups C10G9/00 - C10G69/14
  • C10G2400/30—Aromatics
• • C—CHEMISTRY; METALLURGY
  • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
  • C10L—FUELS 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
  • C10L1/00—Liquid carbonaceous fuels
  • C10L1/04—Liquid carbonaceous fuels essentially based on blends of hydrocarbons
  • C10L1/08—Liquid carbonaceous fuels essentially based on blends of hydrocarbons for compression ignition
• • C—CHEMISTRY; METALLURGY
  • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
  • C10L—FUELS 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
  • C10L1/00—Liquid carbonaceous fuels
  • C10L1/10—Liquid carbonaceous fuels containing additives
• • C—CHEMISTRY; METALLURGY
  • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
  • C10L—FUELS 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
  • C10L10/00—Use of additives to fuels or fires for particular purposes
  • C10L10/14—Use of additives to fuels or fires for particular purposes for improving low temperature properties
• • C—CHEMISTRY; METALLURGY
  • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
  • C10L—FUELS 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
  • C10L2200/00—Components of fuel compositions
  • C10L2200/04—Organic compounds
• • C—CHEMISTRY; METALLURGY
  • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
  • C10L—FUELS 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
  • C10L2200/00—Components of fuel compositions
  • C10L2200/04—Organic compounds
  • C10L2200/0461—Fractions defined by their origin
  • C10L2200/0469—Renewables or materials of biological origin
  • C10L2200/0492—Fischer-Tropsch products
• • C—CHEMISTRY; METALLURGY
  • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
  • C10L—FUELS 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
  • C10L2270/00—Specifically adapted fuels
  • C10L2270/02—Specifically adapted fuels for internal combustion engines
  • C10L2270/026—Specifically adapted fuels for internal combustion engines for diesel engines, e.g. automobiles, stationary, marine

Definitions

• the present invention relates to a gas oil composition, in particular to a gas oil composition which can be used in a very low temperature environments.
• a gas oil composition is produced by blending one or more types of blendstocks produced by subjecting a straight gas oil or straight kerosene, produced through an atmospheric distillation unit of crude oil to hydrorefining or hydrodesulfurization.
• a straight gas oil or straight kerosene produced through an atmospheric distillation unit of crude oil to hydrorefining or hydrodesulfurization.
• the blend ratio of the foregoing kerosene blendstock and gas oil blendstock is controlled in order to ensure low temperature fluidity during a winter season.
• the blendstocks are blended with additives such as cetane number improvers, detergents, and cold flow improvers.
• Fischer Tropsch synthetic oil obtained by Fischer Tropsch synthesis using carbon monoxide and hydrogen as feedstocks, as one of alternative fuels for a petroleum-based fuel is considered.
• gas oil for diesel fuel is produced from FT synthetic oil, gas oil free of sulfur content can be obtained.
• the FT synthetic gas oil is preferable in terms of reducing environmental impact.
• the above-described FT synthetic oil has a relatively high content of straight-chain saturated hydrocarbon (normal paraffin) compounds. It has been pointed out that in particular when heavy normal paraffin compounds are contained, there is the possibility that they would deposit in the form of wax. Further, the FT synthetic blendstock is a hydrocarbon mixture containing predominantly the aforesaid normal paraffin and saturated hydrocarbons having a side chain (isoparaffin) and thus generally has poor oil solubility. Accordingly, there is a case that additives to be dissolved in fuel oils such as gas oil, highly relying on their oil soluble groups (straight-chain alkyl group or the like) would be hardly dissolved. With this being the situation, there has been a problem in that gas oil derived from FT synthetic oil cannot be used in a low temperature environment.
• JP 2007-270109 A discloses a technique of adding and mixing a lubrication improver and a cold flow improver to and with a FT synthetic gas oil composition having a certain composition to thereby improve the fluidity in a low temperature environment.
• the kinetic viscosity at 30° C. is required to be high.
• the pour point is required to be low. In short, since there is a trade-off between the favorable kinetic viscosity and the favorable pour point, it has been difficult to achieve the both using conventional techniques. Therefore, it is desirable to develop a technique making it possible to improve the fluidity without reducing the kinetic viscosity even in a severe low temperature environment.
• the present invention was made in view of the above circumstances, and an object thereof is to provide a gas oil composition that provides superior low temperature performance as compared with the conventional techniques even if it contains as a feedstock, an oil having a high normal paraffin content, such as an FT synthetic oil.
• the inventors of the present invention made various studies on the above problem to find that excellent fluidity in a low temperature environment can be realized without reducing the kinetic viscosity, by optimizing the composition of a gas oil composition and also adding a certain amount of a cold flow improver to the gas oil composition.
• gas oil composition comprise a cold flow improver at 20 ppm to 1000 ppm by mass.
• the present invention makes it possible to provide a gas oil composition providing superior low temperature performance as compared with the case of using the conventional techniques even if an oil having a high normal paraffin content is used as a feedstock.
• a gas oil composition of the present invention has a sulfur content of 1 ppm by mass or less, an aromatic content of 1% by mass or less, a C5-C15 paraffin content of 30% to 85% by mass, a C20-C27 paraffin content of 3% to 20% by mass, and an isoparaffin content of 50% to 75 by mass; and contains 20 ppm to 1000 ppm by mass of a cold flow improver.
• the gas oil composition of the present invention has a sulfur content of 1 ppm by mass or less and an aromatic content of 1 by mass or less.
• the sulfur content is 1 ppm by mass or less and the aromatic content is 1% by mass or less.
• the gas oil composition of the present invention has a C5-C15 paraffin content of 30% to 85% by mass, preferably 40% to 70% by mass.
• the C5-C15 paraffin content is limited to 30% by mass or more in terms of improving the startability of a diesel engine and the stability in idling, and is limited to 85% by mass or less in terms of reducing the particulates emitted from the diesel engine.
• the gas oil composition of the present invention has a C20-C27 paraffin content of 3% to 20% by mass, preferably 7% to 16% by mass.
• the C20-C27 paraffin content needs to be 3% by mass or more for favorable solubility of the cold flow improver, and needs to be 20% by mass or less for favorable low temperature fluidity of the gas oil composition.
• the gas oil composition of the present invention has an isoparaffin content of 50% to 75% by mass, preferably 60% to 70% by mass.
• the isoparaffin content needs to be 50% by mass or more, whereas in order to obtain a gas oil composition with high yield, the isoparaffin content needs to be 75% by mass or less.
• the mass ratio of the normal paraffin content with respect to the isoparaffin content is preferably in the range of 0.3 to 1.0, more preferably in the range of 0.4 to 0.7.
• the mass ratio is preferably 0.3 or more. Since a certain amount of isoparaffin is contained due to isomerization in order to achieve favorable startability and operability at low temperatures, the mass ratio is preferably 1.0 or less.
• the gas oil composition of the present invention preferably has a 5% distillation temperature of 140° C. to 200° C., more preferably 150° C. to 195° C.
• the 5% distillation temperature is 140° C. or more, whereas in order to achieve favorable startability and operability at low temperatures, the 5% distillation temperature is preferably 200° C. or less.
• the gas oil composition of the present invention preferably has a 95% distillation temperature of 300° C. to 340° C., more preferably 310° C. to 330° C.
• the 95% distillation temperature is preferably 300° C. or more, whereas in terms of reducing particulates emitted from the diesel engine, the 95% distillation temperature is preferably 340° C. or less.
• the gas oil composition of the present invention preferably has a density at 15° C. of 0.750 g/cm 3 to 0.780 g/cm 3 , more preferably 0.760 g/cm 3 to 0.780 g/cm 3 .
• the density at 15° C. is 0.750 g/cm 3 or more for favorable specific fuel consumption of a diesel engine, and is 0.780 g/cm 3 or less for favorable low temperature fluidity of the gas oil composition.
• the gas oil composition of the present invention preferably has a cloud point of ⁇ 35° C. or less, more preferably ⁇ 55° C. or less so as to withstand the use under very low temperature weather conditions.
• the cloud point used herein means the pour point measured based on JIS K 2269 “Testing method for pour point and cloud point of crude oil and petroleum products”.
• the gas oil composition of the present invention preferably has a kinetic viscosity at 30° C. of 1.5 mm 2 /s to 4.0 mm 2 /s, more preferably 2.0 mm 2 /s to 3.5 mm 2 /s.
• the kinetic viscosity at 30° C. is 1.5 mm 2 /s or more in terms of improving the startability of a diesel engine or the stability in idling, and is preferably 4.0 mm 2 /s or less in terms of reducing particulates emitted from the diesel engine.
• the pour point of the gas oil composition of the present invention is preferably ⁇ 35° C. or less. In order to achieve favorable low temperature fluidity under very low temperature weather conditions, the pour point is preferably ⁇ 35° C. or less, more preferably ⁇ 55° C. or less.
• the pour point need not be lower than necessary, and the pour point is preferably ⁇ 70° C. or more, more preferably ⁇ 66° C. or more in terms of the production cost of the gas oil composition.
• the gas oil composition of the present invention is required to contain 150 ppm to 1000 ppm by mass of a cold flow improver, the content of the cold flow improver is preferably 150 ppm to 500 ppm by mass, more preferably 200 ppm to 300 ppm by mass.
• the content (addition amount) of the cold flow improver is 150 ppm by mass or more in order to prevent a filter of a diesel powered automobile from being plugged in a low temperature situation, and is 1000 ppm by mass or less in terms of the effectiveness of the cold flow improver and the economic efficiency.
• ethylene-vinyl acetate copolymer and/or cold flow improver having a surfactant effect are/is used.
• the cold flow improver having a surfactant effect include one or more selected from copolymers of ethylene and methyl methacrylate, copolymers of ethylene and ⁇ -olefin, chlorinated methylene-vinyl acetate copolymers, alkyl ester copolymers of unsaturated carboxylic acids, esters synthesized from nitrogen-containing compounds having a hydroxyl group and saturated fatty acids and salts of the esters, esters and amide derivatives synthesized from polyhydric alcohols and saturated fatty acids, esters synthesized from polyoxyalkylene glycol and saturated fatty acid, esters synthesized from alkyleneoxide adducts of polyhydric alcohols or partial esters thereof and saturated fatty acids, chlorinated paraffin/naphthalene condensates, alkenyl succinamides,
• the gas oil composition of the present invention preferably contains a lubricity improver at a concentration of 20 mg/L to 300 mg/L, more preferably 50 mg/L to 200 mg/L.
• a lubricity improver at a concentration of 20 mg/L to 300 mg/L, more preferably 50 mg/L to 200 mg/L.
• the addition amount of the lubricity improver being within the range of 20 mg/L to 300 mg/L, the efficacy of the added lubricity improver can be effectively exerted.
• increase in the driving torque of the pump in operation can be suppressed and the wear of the pump can be reduced.
• a lubricity improver containing a compound which comprises a fatty acid and/or a fatty acid ester and has a polar group is used.
• a compound which comprises a fatty acid and/or a fatty acid ester and has a polar group is used.
• any one or more selected from carboxylic acid-, ester-, alcohol- and phenol-based lubricity improvers can be used. Out of those, carboxylic acid- and ester-based lubricity improvers are preferred.
• carboxylic acid-based lubricity improver examples include linoleic acid, oleic acid, salicylic acid, palmitic acid, myristic acid or hexadecenoic acid or a mixture of two or more of these carboxylic acids.
• Carboxylic acid esters of glycerin can be given as an example of the ester-based lubricity improver.
• the carboxylic acid ester may include one or more carboxylic acids.
• Specific examples of the carboxylic acids include linoleic acid, oleic acid, salicylic acid, palmitic acid, myristic acid, and hexadecenoic acid.
• the weight-average molecular weight of the active component of the lubricity improver is preferably 200 or more and 1000 or less in order to enhance the solubility to the gas oil composition.
• other known fuel oil additives mentioned later may be used alone or in combination.
• the other additives include phenolic- and aminic-antioxidants; metal deactivators such as salicyliden derivatives; anti-corrosion agents such as aliphatic amines and alkenyl succinic acid esters; anti-static additives such as anionic, cationic, and amphoteric surfactants; coloring agents such as azo dye; silicone-based antifoaming agents and antifreezing agents such as 2-methoxyethanol, isopropyl alcohol, and polyglycol ethers.
• the amounts of the other additives may be set to any value. Especially, the amount of each of the other additives is preferably 0.5% by mass or less, more preferably 0.2% by mass or less, on the basis of the total amount of the gas oil composition.
• the gas oil composition of the present invention preferably further contains Fischer Tropsch synthetic oil (FT synthetic oil).
• FT synthetic oil contains a relatively large amount of straight-chain saturated hydrocarbon (normal paraffin) compounds and accordingly, a gas oil derived from an FT synthetic oil cannot be used in a low temperature environment, which has been a problem.
• the advantageous effect of the present invention can be exerted most significantly.
• the gas oil composition preferably contains an FT synthetic oil.
• the FT synthetic oil can be obtained by a production method including the steps of fractionating an FT synthesis oil into a light fraction and a wax fraction, hydroisomerizing the light fraction to obtain a hydroisomerized oil, hydrocracking the wax fraction to obtain a hydrocracked oil, mixing the hydroisomerized oil and the hydrocracked oil and then supplying it to a product fractionator, and adjusting the cutting temperature at the product fractionator so as to obtain a kerosene composition of the invention.
• the light gas oil blendstock and a heavy gas oil blendstock obtained from the product fractionator may be mixed at a predetermined ratio, thereby producing a gas oil composition of the present invention.
• the light gas oil blendstock and the heavy gas oil blendstock have a sulfur content of 1 ppm by mass or less and an aromatic content of 1% by mass or less.
• the light gas oil blendstock preferably has a density of 0.740 to 0.760, a 5% distillation temperature of 155° C. to 175° C.; a 95% distillation temperature of 230° C. to 250° C., a C5-C15 paraffin content of 90% to 99.9% by mass, and an isoparaffin content of 40% to 55% by mass.
• the heavy gas oil blendstock preferably has a density of 0.770 to 0.790, a 5% distillation temperature of 240° C. to 260° C., a 95% distillation temperature of 330° C. to 350° C., a C5-C15 paraffin content of 15% to 35% by mass, and an isoparaffin content of 70% to 85% by mass.
• Paraffin content, isoparaffin content the paraffin content and isoparaffin content per carbon atom were measured using GC-FID. The calculation was performed using values measured using a temperature program (column oven temperature: heated at 8° C./min from 140° C. to 355° C., sample injection temperature: 360° C., detector temperature: 360° C.) at a carrier gas (helium) flow rate of 1.0 mL/min using a nonpolar column (stainless steel capillary column ULTRA ALLOY-1) and an FID (flame ionization detector).
• a temperature program column temperature: heated at 8° C./min from 140° C. to 355° C.
• sample injection temperature 360° C.
• detector temperature 360° C.
• carrier gas flow rate 1.0 mL/min using a nonpolar column (stainless steel capillary column ULTRA ALLOY-1) and an FID (flame ionization detector).
• a light gas oil blendstock and a heavy gas oil blendstock were prepared in accordance with the following procedure.
• composition of the obtained light gas oil blendstock 1 and the heavy gas oil blendstock 1 is shown in Table 1.
• Light gas oil blendstocks and heavy gas oil blendstocks were mixed based on the mixing ratios shown in Table 1.
• a cold flow improver (Infineum R240 manufactured by Infineum Japan Ltd.) was added at 200 ppm by mass to the mixture, thereby obtaining gas oil compositions used as samples.
• Example 2 Example 3
• Example 4 Example 1
• Example 2 Light gas oil blendstock vol % 20 40 60 80 0 100
• Heavy gas oil blendstock vol % 80 60 40 20 100 0 CFI
• Addition amount mass ppm 200 200 200 200 5% Distillation temperature ° C. 187.5 252 165 50% Distillation temperature ° C. 251 293.5 197 95% Distillation temperature ° C. 322 339 238 97% Distillation temperature ° C.
• the present invention has particularly advantageous effects in that a gas oil composition providing superior low temperature performance as compared with the case of using the conventional techniques can be provided and an oil having a high normal paraffin content, such as FT synthetic oil can easily be used as a feedstock of the gas oil composition.

Landscapes

• 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)
• Health & Medical Sciences (AREA)
• Emergency Medicine (AREA)
• Combustion & Propulsion (AREA)
• Liquid Carbonaceous Fuels (AREA)
• Lubricants (AREA)
• Cosmetics (AREA)

Applications Claiming Priority (3)

Publications (1)

Family

ID=49258861

Family Applications (1)

Country Status (11)

Citations (4)

Family Cites Families (8)

• 2013
  • 2013-02-20 KR KR1020147030407A patent/KR20150001788A/ko not_active Application Discontinuation
  • 2013-02-20 US US14/389,597 patent/US20150052803A1/en not_active Abandoned
  • 2013-02-20 RU RU2014137429A patent/RU2630225C1/ru not_active IP Right Cessation
  • 2013-02-20 AU AU2013238990A patent/AU2013238990B2/en not_active Ceased
  • 2013-02-20 MY MYPI2014002600A patent/MY164150A/en unknown
  • 2013-02-20 EP EP13770302.1A patent/EP2832829B1/en not_active Not-in-force
  • 2013-02-20 CN CN201380017657.2A patent/CN104220567B/zh not_active Expired - Fee Related
  • 2013-02-20 JP JP2014507363A patent/JP6042874B2/ja not_active Expired - Fee Related
  • 2013-02-20 SG SG11201406015XA patent/SG11201406015XA/en unknown
  • 2013-02-20 WO PCT/JP2013/000948 patent/WO2013145535A1/ja active Application Filing
• 2014
  • 2014-09-18 ZA ZA2014/06836A patent/ZA201406836B/en unknown

Patent Citations (4)

Also Published As

Similar Documents

Legal Events