CN105567346A - High-definition test oil and preparation method thereof - Google Patents

High-definition test oil and preparation method thereof Download PDF

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Publication number
CN105567346A
CN105567346A CN201610080656.8A CN201610080656A CN105567346A CN 105567346 A CN105567346 A CN 105567346A CN 201610080656 A CN201610080656 A CN 201610080656A CN 105567346 A CN105567346 A CN 105567346A
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test oil
high definition
oil
definition test
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CN105567346B (en
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訾立钧
容永源
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Beijing Zhongyan Hengcheng Energy Co. Ltd.
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Beijing Zhongyuancheng Energy Technology Co 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
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/04Liquid carbonaceous fuels essentially based on blends of hydrocarbons
    • 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
    • C10L10/00Use of additives to fuels or fires for particular purposes
    • C10L10/08Use of additives to fuels or fires for particular purposes for improving lubricity; for reducing wear
    • 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
    • C10L1/182Organic compounds containing oxygen containing hydroxy groups; Salts thereof
    • C10L1/183Organic compounds containing oxygen containing hydroxy groups; Salts thereof at least one hydroxy group bound to an aromatic carbon atom
    • C10L1/1835Organic compounds containing oxygen containing hydroxy groups; Salts thereof at least one hydroxy group bound to an aromatic carbon atom having at least two hydroxy substituted non condensed benzene rings
    • 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
    • C10L1/19Esters ester radical containing compounds; ester ethers; carbonic acid esters
    • 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
    • C10L1/232Organic compounds containing nitrogen containing nitrogen in a heterocyclic ring
    • C10L1/233Organic compounds containing nitrogen containing nitrogen in a heterocyclic ring containing nitrogen and oxygen in the ring, e.g. oxazoles
    • 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
    • C10L1/24Organic compounds containing sulfur, selenium and/or tellurium
    • C10L1/2462Organic compounds containing sulfur, selenium and/or tellurium 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
    • C10L2230/00Function and purpose of a components of a fuel or the composition as a whole
    • C10L2230/08Inhibitors
    • C10L2230/081Anti-oxidants
    • 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
    • C10L2230/00Function and purpose of a components of a fuel or the composition as a whole
    • C10L2230/08Inhibitors
    • C10L2230/085Metal deactivators
    • 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
    • C10L2230/00Function and purpose of a components of a fuel or the composition as a whole
    • C10L2230/20Function and purpose of a components of a fuel or the composition as a whole for improving conductivity

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  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Engineering & Computer Science (AREA)
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  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Lubricants (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Abstract

The invention relates to high-definition test oil and a preparation method thereof. The high-definition test oil is mainly prepared from, by weight, 10-20 parts of liquid paraffin and 2-8 parts of solvent oil. The preparation method comprises the steps of adding the materials into a blending tank according to the proportion and performing even mixing. The high-definition test oil is stable in quality and high in cleanliness, meanwhile has very good oxidation stability and low-temperature startability and can meet the use and testing requirements under the harsh environmental conditions. The preparation method has the advantages that operation is easy and convenient, and the finished product is stable.

Description

A kind of high definition test oil and preparation method thereof
Technical field
The invention belongs to petroleum products technical field, be specifically related to a kind of high definition test oil and preparation method thereof.
Background technology
When new car rolls off the production line, often need to inject a certain amount of fuel oil, i.e. first charge of oil, because new car is from rolling off the production line, to sending in user's hand, the long period may be needed, and the area of Different climate condition sold to by vehicle, therefore just charge of oil may deposit the long time in new car fuel tank, and may stand the test of high temperature, severe cold area condition.If just charge of oil poor quality, poor stability, be then easy to go bad at new car prime the fuel system internal oxidition, produce colloid, and parts such as blocking fuel screen, oil nozzle etc., cause motor fault.In addition, if vehicle is in severe cold area, due to oil product long-term frozen, vehicle may not easily start.Further, the oil product of long-term storage also easily corrodes prime the fuel system, and erosion blocking filter screen and oil nozzle, cause motor fault.
In addition, car manufactures or research and development institution need use-testing oil at motor car engine, car load research and development, test and inner timing signal, and the accuracy of quality to test result of test oil has considerable influence.
Present inventor is when using existing diesel oil as first charge of oil and test oil, find that existing diesel oil is inadequate as stability, degree of cleaning, oxidation stability and low-temperature startup during first charge of oil, the requirement used under the harsh environmental conditions of different areas can not be met, and when as test oil, also because degree of cleaning, oxidation stability are not enough, the requirement of test oil cannot be met.
Summary of the invention
In order to solve the problems referred to above that prior art exists, the invention provides a kind of high definition test oil and preparation method thereof, described high definition test oil steady quality, degree of cleaning are high, there is good oxidation stability and low-temperature startup simultaneously, can meet and use and test requirements document under harsh environmental conditions; Described preparation method has easy and simple to handle, that finished product is stable advantage.
The technical solution adopted in the present invention is: a kind of high definition test oil, and the raw material primarily of following weight part is made: whiteruss 10-20 part and solvent oil 2-8 part.
Preferably, described whiteruss comprises whiteruss 2#, light paraffinic and middle matter paraffin, and the mass ratio of wherein said whiteruss 2#, light paraffinic and middle matter paraffin is 40-60:20-30:20-30.
It should be noted that, the whiteruss 2# described in the present invention, light paraffinic and middle matter paraffin are all name voluntarily according to property of raw material in invention, are not the common names in industry, and the scope of each raw material limits, and is all as the criterion with the content described in specification sheets.
In the present invention, described whiteruss and solvent oil are synthesized by F-T synthesis, F-T synthesis (Fischer-Tropschsynthesis) is one of ICL for Indirect Coal Liquefaction technology, take synthetic gas as the technological process that raw material synthesizes the liquid fuel based on paraffinic hydrocarbon under catalyzer (mainly iron system) and appropriate reaction condition.Its reaction process can represent with following formula: nCO+2nH 2-→ [-CH 2-] n+nH 2o.
The technical process of F-T synthesis mainly comprises the parts such as gasification, gas sweetening, conversion and reformation, synthesis and product purification upgrading.Hydrogen in synthetic gas and the mol ratio of carbon monoxide require at 2-2.5.Reactor adopts fixed bed or fluidized-bed two kinds of forms.Temperature of reaction 320-340 DEG C, pressure 2.0-2.2MPa.Product consists of methane 11%, C2-C4 hydrocarbon 33%, C5-C8 hydrocarbon 44%, more than C9 hydrocarbon 6%, and oxygenatedchemicals 6%.
Adopt the advantage of F-T synthesis to be: adopt that the Determination of Alkane Content in the whiteruss of F-T synthesis and solvent oil is high, cetane value is high, cold filter clogging temperature and zero pour low, the elements such as basic aromatic free and sulphur, nitrogen, oxygen, the more general petroleum products of quality more high-quality.
Described high definition test oil is compared with common diesel: during as test oil, delay period shortens 14-30%, premixed combustion exothermic peak is lower, maximum combustion pressure is lower slightly, legislation discharge and non-regulation noxious emission are obtained for and significantly reduce, and wherein NOx and PM on average reduces 13% and 26% respectively.For diesel motor or car load emission testing, the indexs such as the oxynitrides in tail gas, hydrocarbon polymer, carbon monoxide and particulate pollutant can reach state five emission standard completely; When for first charge of oil, have good effect for guarantee new car prime the fuel system and motor performance, exhaust emissions reaches Europe V standard.
It should be noted that, because of the premium properties of the test oil of high definition described in the present invention, described high definition test oil also can be applied and use as first charge of oil.
Preferably, described high definition test oil also comprises following raw material: static inhibitor, anti-wear agent, oxidation inhibitor and metal passivator.
Vapour, diesel oil easily produce electrostatic accumulation in production, handling and transportation, when electrostatic accumulation is to a certain amount of, easily cause fire failure.Add micro-static inhibitor, the conductivity of oil product can be improved, in time electrostatic is derived, can electrostatic accumulation be prevented, avoid fire failure; Anti-wear agent, for improving the abrasion resistance of oil product, reduces the wearing and tearing of oil pump; Oxidation inhibitor can increase the oxidation stability of described high definition test oil; Described metal passivator can form inert coating or form inner complex with metal ion in metallic surface, stop burning, there is the catalysis booster action suppressing metal on oxidative reaction, simultaneously, demonstrate excellent synergism with appropriate amount and oxidation inhibitor compound, greatly reduce the consumption of oxidation inhibitor.
Preferably, the weight part of described static inhibitor, anti-wear agent, oxidation inhibitor and metal passivator is: static inhibitor 0.0002-0.002 part, anti-wear agent 0.02-0.03 part, oxidation inhibitor 0.02-0.03 part, metal passivator 0.002-0.003 part.
Preferably, described whiteruss 2# is alkanes mixture, and initial boiling point is not less than 175 DEG C, T5 is not less than 185 DEG C, final boiling point is not more than 295 DEG C; Zero pour is not higher than-45 DEG C; Sulphur content is not more than 5ppm; Carbon number distribution is C7-C22; Isomeric alkane content is not less than 85%; N-alkanes content is not more than 15%.
Preferably, described solvent oil is No. 130 solvent oils, is alkane and cycloalkane mixture, and initial boiling point is not less than 260 DEG C, T5 is not less than 265 DEG C, final boiling point is not more than 298 DEG C; Zero pour is not higher than-20 DEG C; Sulphur content is not more than 5ppm; Bromine index is not more than 50mgBr/100g.
Preferably, described light paraffinic is alkanes mixture, and initial boiling point is not less than 168 DEG C, T50 is not less than 225 DEG C, T90 is not less than 270 DEG C, T95 is not less than 280 DEG C, final boiling point is not more than 290 DEG C; Zero pour is not higher than-25 DEG C; Sulphur content is not more than 6ppm; Cetane index is not less than 50.
Preferably, described middle matter paraffin is alkanes mixture, and initial boiling point is not less than 168 DEG C, T50 is not less than 250 DEG C, T90 is not less than 305 DEG C, T95 is not less than 320 DEG C, final boiling point is not more than 330 DEG C; Zero pour is not higher than-30 DEG C; Sulphur content is not more than 6ppm; Cetane index is not less than 70.
It should be noted that, T5, T50, T90, T95 described in the present invention is the general distillation term of petroleum industry: T5 represents overhead product and accounts for temperature when cumulative volume is 5%, T50 represents overhead product and accounts for temperature when cumulative volume is 50%, T90 represents overhead product and accounts for temperature when cumulative volume is 90%, and T95 represents overhead product and accounts for temperature when cumulative volume is 95%.
Preferably, described static inhibitor is the ashless diesel oil static inhibitor of polysulfones/polyamine type; Water separation index is not less than 70, and specific conductivity is not less than 200ps/m.
Preferably, described anti-wear agent is fatty acid ester anti-wear agent, its acid number is not more than 2mgKOH/g, condensation point is not higher than-16 DEG C, sulphur content is not more than 100mg/kg, as R665, unit becomes in Beijing the CY102D of profit English connection, is that lipid acid and the polyvalent alcohol of 12-18 is raw material with carbonatoms, under catalyst action, carry out esterification, obtain the polyol esters of fatty acids of purity more than 95%.
Preferably, described oxidation inhibitor is 2,6 ditertiary butyl p cresol, and its first fusing point is 69-70 DEG C, free cresols is not more than 0.015% (m/m).2,6 ditertiary butyl p cresol adopts p-cresol and iso-butylene to be the oil dope that raw material obtains, and this agent oil soluble is good, water insoluble and caustic soda.
Preferably, described metal passivator is 124 Triazole derivative, and 20 DEG C of density are 910-1040kg/m3,50 DEG C of kinematic viscosity 10-14mm 2/ s, base number 210-230mgKOH/g, oxidation test (increment) are not less than 90min.
It should be noted that, the first charge of oil in the present invention is mechanicals, is raw materials usedly commercially available industrial raw material or the satisfactory raw material of homemade parameter.Although Industrial products are generally mixture, as long as meet described parameter, just can ensure final final product quality, so the protection domain exceeding application claims can not be considered as.
Present invention also offers a kind of preparation method of described high definition test oil, comprise the following steps:
Described raw material is added in Mixer pot according to aforementioned proportion, mixes.
Because the raw material major part that the present invention adopts is commercially available industrial raw material, different brands and batch raw material, even if model is the same, also qualitative fluctuation is had, think and ensure the quality of final finished, preparation method in the present invention contains the step of detection: after mixing, and then samples, analyze qualified after namely obtain described high definition test oil.
If no special instructions, in the present invention, all parts, per-cent are weight unit, and all equipment and raw material etc. all can be buied from market or the industry is conventional.
Beneficial effect of the present invention is:
1, the invention provides a kind of high definition test oil, described high definition test oil steady quality, degree of cleaning are high, have good oxidation stability and low-temperature startup simultaneously, can meet and use and test requirements document under harsh environmental conditions.
2, when the high definition test oil in the present invention is as test oil, delay period shortens 14-30%, and premixed combustion exothermic peak is lower, and maximum combustion pressure is lower slightly, legislation discharge and non-regulation noxious emission are obtained for and significantly reduce, and wherein NOx and PM on average reduces 13% and 26% respectively.For diesel motor or car load emission testing, the indexs such as the oxynitrides in tail gas, hydrocarbon polymer, carbon monoxide and particulate pollutant can reach state five emission standard completely; When for first charge of oil, have good effect for guarantee new car prime the fuel system and motor performance, exhaust emissions reaches Europe V standard.
3, the first charge of oil component in the present invention is totally pure, objectionable impurities as: harmful metal elements, sulphur, phosphorus, chlorine, mechanical impurity particle equal size are extremely low, and thus oil corrosion is extremely low, and detergency is fine, are conducive to protection engine using function.
4, the first charge of oil in the present invention, raw material is easy to get, and can directly buy from market.
5, the preparation method in the present invention, has easy and simple to handle, that finished product is stable advantage.
Embodiment
Below in conjunction with embodiment, further illustrate content of the present invention.Should be appreciated that enforcement of the present invention is not limited to the following examples, any pro forma accommodation make the present invention and/or change all will fall into scope.
In the present invention, if not refer in particular to, all parts, per-cent are weight unit, and all equipment and raw material etc. all can be buied from market or the industry is conventional.Method in following embodiment, if no special instructions, is the ordinary method of this area.
Tabulate kind and the consumption of embodiment 1-6 Raw below, specifically refer to table 1
Table 1: embodiment 1-6 materials table
According to the materials of component each in upper table, be prepared as follows:
Described raw material is added in Mixer pot according to aforementioned proportion, mixes, then sample, analyze qualified after namely obtain described high definition test oil.
It should be noted that, raw material used meets the parameter request of specification sheets.In addition, in embodiment 4 and 5: described static inhibitor is Ashless type static inhibitor T1502, described anti-wear agent is the R665 of profit English connection; Static inhibitor used in embodiment 6 is Ashless type static inhibitor T1503, and described anti-wear agent is the CY102D that in Beijing, unit becomes; In embodiment 4-6, described oxidation inhibitor is T501, and described metal passivator is T551.
In order to verify the quality product of just charge of oil in the present invention further, spy does following detection, and concrete detected result is in table 2:
Table 2: detected result table
As can be seen from Table 1 and Table 2, within the scope of each amounts of components given by the present invention, the high-quality oil product of indices equilibrium can be obtained.This oil product has following outstanding advantages:
1, in described high definition test oil due to the oxidation inhibitor introduced and metal passivator, thus have good thermostability and oxidation-resistance, not easily produce colloid and so on objectionable impurities, ensure that sealing deposits more than 1 year, oil product never degenerates;
2, the overall fraction of described high definition test oil is partially lighter than ordinary diesel oil, and has extremely low cold filter clogging temperature, and thus low-temperature startup is very good, is particularly suitable for severe cold area use in winter, ensures that vehicle launch is smooth and easy;
3, the component in described high definition test oil is very pure, and substantially without alkene and aromatic hydrocarbons, objectionable impurities (metallic element, sulphur, particulate matter) content is extremely low, and thus oil corrosion is extremely low, and detergency is fine, is conducive to protecting engine.
With example 6 scheme implementation industrial production, the multiple batches of examination and test of products the results are shown in Table 3.
Table 3: different batches detected result table
From different production batch, quality product is highly stable, industrial production from 30 days June in 2015, to having produced 12 batches at present.
Certain Automobile Enterprises domestic carries out emission testing under the same test conditions with state five diesel oil that oil, Plant of Tianjin Petrochemical Company and Yanshan Petrochemical are tested in the Europe five of the high definition test oil in the present invention, European import respectively, and test-results is in table 4.
Table 4: emission testing detected result table
As shown in Table 4, compared with the 0# diesel oil of European Europe five, Plant of Tianjin Petrochemical Company and the Yanshan Petrochemical state five 0# oil product each pollutant effect to discharge is all higher, has the greatest impact, can think that the state five 0# oil product of above-mentioned Liang Ge company is not useable for emission testing thus to CO; High definition test oil in the present invention is higher 9.16% to NOx, PM is on the low side 53.75%, and all the other discharge pollutants and can be considered without impact, can think that this oil product can be used for emission testing thus.
It should be noted last that; above embodiment is only in order to illustrate technical scheme of the present invention and unrestricted; although with reference to preferred embodiment to invention has been detailed description; be understood that; the foregoing is only the specific embodiment of the present invention, the protection domain be not intended to limit the present invention, within the spirit and principles in the present invention all; any amendment of making, equivalent replacement, improvement etc., all should be included within protection scope of the present invention.

Claims (10)

1. a high definition test oil, is characterized in that, the raw material primarily of following weight part is made: whiteruss 10-20 part and solvent oil 2-8 part.
2. high definition test oil according to claim 1, is characterized in that, described whiteruss comprises whiteruss 2#, light paraffinic and middle matter paraffin, and the mass ratio of wherein said whiteruss 2#, light paraffinic and middle matter paraffin is 40-60:20-30:20-30.
3. high definition test oil according to claim 1 and 2, is characterized in that, also comprises following raw material: static inhibitor, anti-wear agent, oxidation inhibitor and metal passivator.
4. high definition test oil according to claim 3, it is characterized in that, the weight part of described static inhibitor, anti-wear agent, oxidation inhibitor and metal passivator is: static inhibitor 0.0002-0.002 part, anti-wear agent 0.02-0.03 part, oxidation inhibitor 0.02-0.03 part and metal passivator 0.002-0.003 part.
5. according to the arbitrary described high definition test oil of claim 2-4, it is characterized in that, described whiteruss 2# is alkanes mixture, and initial boiling point is not less than 175 DEG C, T5 is not less than 185 DEG C, final boiling point is not more than 295 DEG C; Zero pour is not higher than-45 DEG C; Sulphur content is not more than 5ppm; Carbon number distribution is C7-C22; Isomeric alkane content is not less than 85%; N-alkanes content is not more than 15%.
6. according to the arbitrary described high definition test oil of claim 1-4, it is characterized in that, described solvent oil is No. 130 solvent oils, is alkane and cycloalkane mixture, and initial boiling point is not less than 260 DEG C, T5 is not less than 265 DEG C, final boiling point is not more than 298 DEG C; Zero pour is not higher than-20 DEG C; Sulphur content is not more than 5ppm; Bromine index is not more than 50mgBr/100g.
7. according to the arbitrary described high definition test oil of claim 2-4, it is characterized in that, described light paraffinic is alkanes mixture, and initial boiling point is not less than 168 DEG C, T50 is not less than 225 DEG C, T90 is not less than 270 DEG C, T95 is not less than 280 DEG C, final boiling point is not more than 290 DEG C; Zero pour is not higher than-25 DEG C; Sulphur content is not more than 6ppm; Cetane index is not less than 50.
8. according to the arbitrary described high definition test oil of claim 2-4, it is characterized in that, described middle matter paraffin is alkanes mixture, and initial boiling point is not less than 168 DEG C, T50 is not less than 250 DEG C, T90 is not less than 305 DEG C, T95 is not less than 320 DEG C, final boiling point is not more than 330 DEG C; Zero pour is not higher than-30 DEG C; Sulphur content is not more than 6ppm; Cetane index is not less than 70.
9. the high definition test oil according to claim 3 or 4, is characterized in that, described static inhibitor is the ashless diesel oil static inhibitor of polysulfones/polyamine type; Described anti-wear agent is fatty acid ester anti-wear agent; Described oxidation inhibitor is 2,6 ditertiary butyl p cresol; Described metal passivator is 124 Triazole derivative.
10. a preparation method for the high definition test oil described in claim 1-4, is characterized in that, comprise the following steps:
Described raw material is added in Mixer pot according to aforementioned proportion, mixes.
CN201610080656.8A 2016-02-04 2016-02-04 High-definition test oil and preparation method thereof Active CN105567346B (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108329957A (en) * 2018-04-25 2018-07-27 河北帅征清洁能源有限公司 It is suitble to the derv fuel and preparation method thereof of highlands

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20040030205A1 (en) * 2002-05-24 2004-02-12 Eni S.P.A. Essentially hydrocarbon compositions to be used as fuels with enhanced lubricating properties
CN101283077A (en) * 2005-08-22 2008-10-08 国际壳牌研究有限公司 A diesel fuel and a method of operating a diesel engine
US20090101541A1 (en) * 2006-03-31 2009-04-23 Yasutoshi Iguchi Light oil compositions
CN101517044A (en) * 2006-07-27 2009-08-26 国际壳牌研究有限公司 Fuel compositions
CN101885997A (en) * 2009-05-13 2010-11-17 通用汽车环球科技运作公司 Synthetic diesel fuel compositions

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20040030205A1 (en) * 2002-05-24 2004-02-12 Eni S.P.A. Essentially hydrocarbon compositions to be used as fuels with enhanced lubricating properties
CN101283077A (en) * 2005-08-22 2008-10-08 国际壳牌研究有限公司 A diesel fuel and a method of operating a diesel engine
US20090101541A1 (en) * 2006-03-31 2009-04-23 Yasutoshi Iguchi Light oil compositions
CN101517044A (en) * 2006-07-27 2009-08-26 国际壳牌研究有限公司 Fuel compositions
CN101885997A (en) * 2009-05-13 2010-11-17 通用汽车环球科技运作公司 Synthetic diesel fuel compositions
US20100287819A1 (en) * 2009-05-13 2010-11-18 Gm Global Technology Operations, Inc. Synthetic diesel fuel compositions

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
杨帅等: "清洁能源GTL柴油作为柴油机代用燃料的试验研究", 《内燃机工程》 *

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108329957A (en) * 2018-04-25 2018-07-27 河北帅征清洁能源有限公司 It is suitble to the derv fuel and preparation method thereof of highlands

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