WO2013023372A1 - A gasoline composition and its preparation method - Google Patents

A gasoline composition and its preparation method Download PDF

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Publication number
WO2013023372A1
WO2013023372A1 PCT/CN2011/078538 CN2011078538W WO2013023372A1 WO 2013023372 A1 WO2013023372 A1 WO 2013023372A1 CN 2011078538 W CN2011078538 W CN 2011078538W WO 2013023372 A1 WO2013023372 A1 WO 2013023372A1
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Prior art keywords
gasoline
weight
sec
butyl acetate
gasoline composition
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PCT/CN2011/078538
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French (fr)
Chinese (zh)
Inventor
李华
刘粮帅
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湖南中创化工股份有限公司
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Priority to JP2014525280A priority Critical patent/JP5981994B2/en
Priority to KR1020147006792A priority patent/KR101700490B1/en
Priority to MYPI2014700323A priority patent/MY171236A/en
Priority to EP11871089.6A priority patent/EP2722383B1/en
Priority to PCT/CN2011/078538 priority patent/WO2013023372A1/en
Publication of WO2013023372A1 publication Critical patent/WO2013023372A1/en

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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
    • C10L1/10Liquid 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
    • C10L1/02Liquid carbonaceous fuels essentially based on components consisting of carbon, hydrogen, and oxygen only
    • C10L1/023Liquid carbonaceous fuels essentially based on components consisting of carbon, hydrogen, and oxygen only for spark ignition
    • 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
    • C10L10/10Use of additives to fuels or fires for particular purposes for improving the octane number
    • 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
    • C10L1/16Hydrocarbons
    • C10L1/1608Well defined compounds, e.g. hexane, benzene
    • 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
    • C10L1/1822Organic compounds containing oxygen containing hydroxy groups; Salts thereof hydroxy group directly attached to (cyclo)aliphatic carbon atoms
    • C10L1/1824Organic compounds containing oxygen containing hydroxy groups; Salts thereof hydroxy group directly attached to (cyclo)aliphatic carbon atoms mono-hydroxy
    • 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
    • C10L1/185Ethers; Acetals; Ketals; Aldehydes; Ketones
    • C10L1/1852Ethers; Acetals; Ketals; Orthoesters
    • 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
    • C10L2200/00Components of fuel compositions
    • C10L2200/04Organic compounds
    • C10L2200/0407Specifically defined hydrocarbon fractions as obtained from, e.g. a distillation column
    • C10L2200/0415Light distillates, e.g. LPG, naphtha
    • C10L2200/0423Gasoline
    • 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
    • C10L2270/00Specifically adapted fuels
    • C10L2270/02Specifically adapted fuels for internal combustion engines
    • C10L2270/023Specifically adapted fuels for internal combustion engines for gasoline engines
    • 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
    • C10L2270/00Specifically adapted fuels
    • C10L2270/02Specifically adapted fuels for internal combustion engines
    • C10L2270/026Specifically adapted fuels for internal combustion engines for diesel engines, e.g. automobiles, stationary, marine

Definitions

  • the present invention relates to a gasoline composition and a process for the preparation thereof, and more particularly to a high octane gasoline composition and a process for the preparation thereof. Background technique
  • octane in gasoline is mainly lead compounds, but due to the serious environmental pollution of lead compounds, China has banned the production of leaded gasoline.
  • the octane number of gasoline can now be increased by adding an aromatic compound, an oxygenate or methylcyclopentadienyl manganese tricarbonyl (MMT) to the gasoline.
  • MMT methylcyclopentadienyl manganese tricarbonyl
  • oxygenates mainly include ether compounds and alcohol compounds, wherein the ether compounds include methyl tert-butyl ether (MTBE), ethyl tert-butyl ether (ETBE) and tert-amyl methyl ether (TAME).
  • MTBE methyl tert-butyl ether
  • ETBE ethyl tert-butyl ether
  • TAME tert-amyl methyl ether
  • MMT methylcyclopentadienyl manganese tricarbonyl
  • MMT is a highly efficient unleaded gasoline antiknock additive that improves both octane and lead. MMT is less popular and less expensive, so it is favored by users. However, the combustion products of MMT will form deposits on the spark plug of the engine, which will deteriorate the combustion conditions; MMT will be easily decomposed by light, which will cause the octane number in the process of gasoline to decrease. At the same time, the manganese-containing waste gas generated serious pollution to the environment, and most developed countries have now banned the use of MMT. China's realistic third-stage motor vehicle emission standards (ie, National III standards) also clearly stipulate that the manganese content of motor gasoline is not more than 0.016g/L.
  • ester compounds as an additive component for increasing the octane number of gasoline.
  • CN1198466A discloses a gasoline additive composition and a method for producing the same, which comprises 0-5.0% by weight of cyclopentadiene, 0.4-1.6% by weight of halogenated olefin, 0-1.5% by weight of halogenated Ethane, 0.3-4.0% by weight of ester, 30.0-65.0% by weight of aromatic hydrocarbon, 0-5.0% by weight of enzyme, 1.0-5.0% by weight of organic acid anhydride, 0-10.0% by weight of castor oil, 30.00-60.0 by weight 5% solvent and 0.001-0.02% by weight dye.
  • the ester has the formula C x COOC y (wherein X is an integer from 1 to 4, and y is an integer from 1 to 3), and may be selected from the group consisting of ethyl acetate, propyl acetate, and butyl acetate.
  • X is an integer from 1 to 4, and y is an integer from 1 to 3
  • the additive composition can increase the octane number of the gasoline, the aromatic hydrocarbon content of the additive composition is high, and therefore, the increase in the octane number of the gasoline substantially benefits from the added aromatic hydrocarbon; and, because of the high aromatic content
  • the additive composition is difficult to meet increasingly stringent environmental standards.
  • the composition of the gasoline additive composition is complicated, the preparation process is cumbersome, and it is not conducive to lowering low cost.
  • CN1513954A discloses a multifunctional fuel and a method for producing the same, the raw material of the multifunctional fuel comprising a main material and an auxiliary material.
  • the main raw materials include: light hydrocarbons, light oil, wood essence, sulfonated oil, coal tar, gasoline and diesel; auxiliary materials including ethyl octadecanoate, ash manganese oxide, sodium hydroxide, water, ethanol, peroxidation Hydrogen, naphthol, petroleum ether, iron cyclopentadienide, acetone, toluene, phytic acid, sec-butyl acetate, butyl valerate, isoamylene, ethyl acetate, calcium hypochlorite, sodium tetraborate , 2-phenylethanol and cyclohexanone.
  • auxiliary materials are composed of four groups of formulas A, B, C and D, which respectively produce a cosolvent, an oxygen enhancer, a combustion improver, a smoke suppressant, an anti-shock anti-vibration agent, an antistatic agent, a preservative and an alkane regulator. .
  • formula of each group of recipes is as follows:
  • Group A ethyl octadecanoate 2-20% by weight, ash manganese oxide 3-15% by weight, sodium hydroxide 2-15% by weight, water 40-80% by weight, ethanol 5-30% by weight;
  • Group B 5-25 wt% of naphthol, 10-30 wt% of petroleum ether, 5-20 wt% of hydrogen peroxide, 5-30 wt% of iron cyclopentadiene, 3-30 wt% of acetone, toluene 5- 30% by weight;
  • Group C Phytic acid 5-25% by weight, sec-butyl acetate 3-30% by weight, butyl valerate 5-30% by weight, Isopenten 10-40% by weight, Ethyl acetate 5-20% by weight, Double Cyanamide 5-40% by weight;
  • Group D dicyclohexylamine 2-20% by weight, calcium hypochlorite 3-30% by weight, sodium tetraborate decahydrate 5-35 wt%,
  • the above four groups of formulas are formulated into a comprehensive additive group E by reaction, and then the group E is added to the main material as needed to prepare a multifunctional fuel.
  • the versatile fuel uses sec-butyl acetate, sec-butyl acetate is added to the multifunctional fuel as an auxiliary agent, and the amount of sec-butyl acetate added is low, wherein sec-butyl acetate The amount added in the multifunctional fuel is less than 0.5% by weight.
  • CN1513954A specifically discloses the production of gasoline engine fuel, 50 parts by weight of No. 70 gasoline, 30 parts by weight of wood essence, 20 parts by weight of No. 120 solvent oil and 0.45 parts of Group E comprehensive additive may be mixed, but The specific performance specifications of the gasoline engine fuel prepared are not disclosed.
  • the main problem of the fuel additive disclosed in CN1513954A is that: the fuel additive has many components, and therefore, the preparation process is complicated and the cost is too high; and the four groups of formulas A, B, C and D contain olefins, and the content of olefins is Higher, it is not conducive to reducing the olefin content of gasoline, so it is not environmentally friendly.
  • EP0905217A discloses an unleaded gasoline containing an oxygen-containing compound having 2 to 15 carbon atoms, the content of the oxygen-containing compound in gasoline being such that the content of oxygen atoms is based on the total amount of gasoline. 0.1-15% by weight.
  • the introduction of the oxygenate can reduce the amount of smoke exhausted from the engine, suppress the smoldering of the spark plug, and reduce the build-up of gasoline in the combustion chamber.
  • the oxygenate may be an ester compound, the examples thereof only disclose gasoline containing methyl tert-butyl ether, tert-amylethyl ether and methoxypropyl acetate, respectively.
  • GB 2,114,596 A discloses a fuel composition comprising 3 to 50% by volume of t-butyl acetate; and specifically discloses a fuel composition comprising 90% by volume of gasoline and 10% by volume of t-butyl acetate.
  • the octane number and motor octane number of the fuel composition are higher than that of the raw material gasoline.
  • t-butyl acetate is relatively expensive and is added as a component of gasoline. uneconomic.
  • the invention is to overcome the deficiencies of the prior art, and to provide a gasoline composition with good antiknocking property, long induction period, low gel content, green environmental protection and low cost, and a preparation method thereof, and the preparation method is simple and convenient to operate. Production costs are low.
  • the gasoline composition according to the present invention contains raw gasoline and sec-butyl acetate, and the content of the sec-butyl acetate is 1 to 30% by weight based on the total amount of the gasoline composition, and the content of the raw gasoline is 70-99% by weight.
  • the method for producing a gasoline composition according to the present invention comprises the step of adding sec-butyl acetate to the raw gasoline, the amount of the sec-butyl acetate added in the gasoline composition based on the total amount of the gasoline composition
  • the content of sec-butyl acetate is from 1 to 30% by weight, and the content of the raw gasoline is from 70 to 99% by weight.
  • the gasoline composition of the present invention employs sec-butyl acetate as an additive (i.e., a blending component).
  • sec-butyl acetate has high octane number, low toxicity, low solubility in water and low cost, especially compared with additives for improving the antiknock property of gasoline.
  • Secondary butyl acetate is a more efficient, environmentally friendly and economical gasoline additive.
  • the sec-butyl acetate in the gasoline composition can improve the octane number and the antiknock index of the existing gasoline, thereby improving the antiknock property of the gasoline.
  • the sec-butyl acetate in the gasoline composition can also function to dilute the aromatics content of the gasoline component, thereby reducing the environmental pollution of the aromatic hydrocarbons.
  • the gasoline composition containing sec-butyl acetate has a long induction period and a low gel content.
  • sec-butyl acetate is inexpensive and does not add to the cost of gasoline.
  • the gasoline octane number of the gasoline composition obtained by adding 9.8% by weight of sec-butyl acetate to the catalytic gasoline is increased from 90.4 to 93.0, and the motor octane number is 81.4 increased to 83.6, the antiknock index increased from 85.9 to 88.3; and the induction period of catalytic gasoline containing 9.8% by weight of sec-butyl acetate was greater than 600 minutes, and the actual colloid content was only 2.77 mg/100 mL.
  • the purity of sec-butyl acetate is not particularly limited and has a good raw material suitability.
  • the use of sec-butyl acetate is flexible, and it can be used not only in place of the existing gasoline additive but also in combination with the existing gasoline additive. That is to say, the gasoline composition provided by the invention has a flexible preparation method, and can be added to the unreconciled gasoline component (such as catalytic gasoline fraction, straight-run gasoline fraction, etc.) obtained in a refinery or a chemical plant. Obtained from the ester, it can also be obtained by adding sec-butyl acetate to the existing finished gasoline, which has a broad spectrum and can comprehensively improve the performance of the raw gasoline in the finished gasoline and unconformed gasoline.
  • the preparation method of the gasoline composition according to the present invention is simple in operation, and does not require a complicated process such as heating and reaction, and the sec-butyl acetate is added to the raw material oil and stirred uniformly.
  • the gasoline composition according to the present invention contains raw gasoline and sec-butyl acetate, and the content of the sec-butyl acetate is 1 to 30% by weight based on the total amount of the gasoline composition, and the content of the raw gasoline is 70-99% by weight.
  • Sec-butyl acetate is a colorless, transparent liquid that is insoluble in water but soluble in most organic solvents.
  • the inventors of the present invention have found that sec-butyl acetate has excellent comprehensive properties and is a good gasoline additive. The following is a detailed description in conjunction with relevant performance indicators. 1, density
  • the density of motor gasoline is generally 0.70-0.78kg/m 3
  • the density of sec-butyl acetate is 0.862kg/m 3
  • the addition of sec-butyl acetate is not applicable to vehicles under the condition of not more than 30% by weight.
  • the density of gasoline causes adverse effects.
  • Octane number is an important indicator for measuring the antiknock resistance of motor gasoline. It is also an important indicator for measuring gasoline additives.
  • the motor octane number and the research octane number are compared under standard conditions with the knocking tendency of the sample with a known octane reference fuel.
  • the reference fuel is isooctane (octane number)
  • the volume percentage of isooctane contained in the reference fuel which is a mixture of n-heptane (zero octane number) and equivalent to the knocking strength of the sample, is the octane number of the sample.
  • the motor octane number is determined according to the provisions of GB/T503
  • the research method octane number is determined according to the provisions of GB/T5487.
  • the method for determining the octane number and the motor octane number is basically the same as that of the device, except that the standard conditions at the time of measurement are different.
  • Motor octane is characterized by harsh conditions of higher gas mixture temperatures (typically heated to 149 ° C) and higher engine speeds (900 r/mi n ⁇ 10 r /min), typically used to measure the throttle in the engine.
  • the research octane number is characterized by moderately harsh conditions of lower mixture temperature (generally not heated) and lower engine speed (600r/min ⁇ 6r/min), which is generally used to assess the transition from low speed to The antiknock of gasoline at medium speed.
  • the octane number of the same gasoline is generally higher than the motor octane number. The following relationship can be used to approximate the values of the two, ⁇ :
  • the difference between the octane number and the motor octane number is called the sensitivity of gasoline.
  • the sec-butyl acetate has a very high octane number, with a research octane number (RON) of 119 and a motor octane number (MON) of 107, which is significantly higher than the commonly used octane number of gasoline. Or additives (Table 1).
  • Both the motor octane number and the research octane number are measured on a dedicated single-cylinder engine under standard test conditions, and it is difficult to fully reflect the antiknock performance of the fuel under vehicle operating conditions. Therefore, the empirical relationship of calculating the antiknock performance under the actual operating conditions of the vehicle is proposed.
  • Anti-explosion index (1 € ⁇ ten MON) / 2
  • the antiknock index is used to reflect the average antiknock performance of gasoline under normal operating conditions. It can be seen from the above formula that the higher the octane number of gasoline, the better its explosion resistance, and the more the engine's power and economy can be reflected.
  • the blast resistance index of sec-butyl acetate was 113, which was also significantly higher than the antiknock index of the gasoline additive listed in Table 1.
  • the evaporation time in the cylinder is only 0.02-0.03s.
  • the indicators reflecting the evaporation performance of gasoline are the distillation range and saturated vapor pressure. In the quality standards for Chinese motor gasoline, the distillation range indicators include 10% by volume evaporation temperature, 50% by volume evaporation temperature, 90% by volume evaporation temperature, and final boiling point ( ⁇ , dry point).
  • the 10% by volume evaporation temperature indicates the amount of low-boiling fraction contained in gasoline, which has a decisive influence on the difficulty of starting the gasoline engine, and is also closely related to the tendency to generate gas resistance.
  • the lower the 10% by volume evaporation temperature the more low-boiling fractions contained in the gasoline and the higher the evaporability, making the gasoline engine easy to start at a low temperature; however, if the evaporation temperature is too low, gas resistance is likely to occur.
  • China's motor gasoline quality standards require that 10% by volume of the evaporation temperature be no higher than 70 °C.
  • the 90% by volume evaporation temperature and the end point indicate the amount of heavy fraction in the gasoline. If the temperature is too high, it indicates that the gasoline contains too much heavy fraction, and it is not easy to ensure complete evaporation and complete combustion of the gasoline under the conditions of use. This will result in an increase in cylinder coke and an increase in fuel consumption. At the same time, the incompletely vaporized heavy fraction of gasoline will also flow into the crankcase, diluting the lubricating oil and increasing wear. In China's automotive gasoline quality standards, 90% of the evaporation temperature is not higher than 190 °C, and the final boiling point is not higher than 205 °C.
  • the sec-butyl acetate has a boiling point of 112.3 ° C and has a certain volatility.
  • the evaporation temperature of 10% by volume and 50% by volume of gasoline slightly increases, and the evaporation temperature of 90% by volume decreases slightly.
  • the evaporation performance of the gasoline composition has a negative impact.
  • the saturated vapor pressure is used to evaluate the evaporation strength of gasoline. It is a measure of whether gasoline is prone to generate gas resistance in a gasoline engine fuel supply system. It can also measure the loss tendency of gasoline in storage and transportation. The greater the saturated vapor pressure of gasoline, the stronger the evaporability, and the engine is prone to cold start, but the tendency to generate gas resistance increases, and the evaporation loss increases. Therefore, when the atmospheric pressure is different from the ambient temperature, the saturated vapor pressure of the gasoline The requirements are also different. The National III standard stipulates that the gasoline vapor pressure is not more than 88 kPa from November 1 to April 30, and is not more than 72 kPa from May 1 to October 31.
  • the induction period refers to the period of time that the oil is in a stable state under the specified accelerated oxidation conditions, and can be measured according to the method specified in GB/T8018.
  • the method is summarized as follows: The sample is oxidized in an oxygen bomb. The oxygen bomb is first oxygenated at 65 ° ⁇ -25 to 68 ⁇ 1 ⁇ 3 ⁇ 4 and then heated to 98 °C -102 °C. Read pressure at regular intervals, or continuously record pressure until the turning point is reached. The time required for the sample to reach the turning point is the measured induction period at the test temperature. From this measured induction period, the induction period at 10 CTC can be calculated. The induction period of gasoline is measured in minutes.
  • the induction period of gasoline is long, and the tendency to oxidize and form colloid is small.
  • the National III standard stipulates that the induction period of gasoline is not less than 480 minutes.
  • the induction period of sec-butyl acetate is greater than 600 minutes, meeting the national III index.
  • the water-soluble acid refers to a mineral acid and a low molecular organic acid
  • the water-soluble alkali refers to sodium hydroxide or the like. They are generally left in the oil refining process and have a strong corrosive effect on metals. They are not allowed in gasoline.
  • the content of water-soluble acid or alkali in gasoline can be determined in accordance with the provisions of GB/T259.
  • the method outline is: extracting the water-soluble acid or alkali in the sample with distilled water or an aqueous solution of ethanol, and then checking the change of the color of the extract with methyl orange or phenolphthalein indicator, respectively, or determining the pH of the extract by using a pH meter Value to determine the presence or absence of a water soluble acid or base.
  • the sec-butyl acetate product is basically free of water-soluble acid and water-soluble alkali, and conforms to relevant Chinese national standards.
  • the refined gasoline produced by the refinery does not contain mechanical impurities and moisture.
  • the gasoline is inevitably polluted by the outside world, causing mechanical impurities and moisture to enter the gasoline.
  • Mechanical impurities in the gasoline may block the carburetor orifice and the fuel filter; it also exacerbates the wear of the carburetor orifice and the cylinder piston assembly.
  • the moisture in the gasoline may freeze in winter. In severe cases, it will block the filter or the oil circuit, and even cause the oil supply to be interrupted.
  • the water also accelerates the corrosion of the parts, dissolves the antioxidants, accelerates the oxidation of the raw rubber, and causes Decomposition of tetraethyl lead causes undesirable effects such as failure of additives such as a propellant.
  • the sample should be placed in a lOOmL glass cylinder for 8-12 hours and should remain transparent and free of suspended and settled mechanical impurities and moisture.
  • the mechanical impurities can be measured according to the method specified in GB/T511; the moisture can be measured according to the method specified in GB/T260. There were no mechanical impurities and moisture suspended and settled in the sec-butyl acetate.
  • the olefin content of motor gasoline should be less than or equal to 30% by volume. Although a small amount of olefins are produced during the production of sec-butyl acetate, the olefin content is low and does not significantly increase the olefin content of the gasoline.
  • Limiting the oxygen content in motor gasoline is mainly a matter of considering the calorific value.
  • the oxygen content in gasoline is increased, the effective component that can be burned in the gasoline is reduced, thereby lowering the calorific value and affecting the power of the engine.
  • the oxygen content in gasoline has passed High, the carbon deposits in the cylinder will be less and less, and the cylinder exhaust valve loses the carbon deposit protection, so the wear will be more serious.
  • the oxygen content in gasoline should be less than 2.7% by weight.
  • the oxygen content of sec-butyl acetate is 27.6% by weight, the gasoline containing sec-butyl acetate can satisfy the regulation of the gasoline standard for automobiles by controlling the amount of sec-butyl acetate added to the gasoline.
  • the actual gum is generally used to illustrate the tendency of gasoline to form deposits on the intake pipe and the intake valve. It is the portion of the gasoline evaporation residue that is insoluble in n-heptane measured under specified conditions. It can be measured according to the provisions of GB/T8019. The method is summarized as follows: The known amount of fuel is evaporated under the conditions of controlled temperature and controlled air, and the residue after pre-heptane extraction and extraction is weighed separately, and the result is The mg/100mL report can be used to measure the actual gum quality of gasoline.
  • the National III standard stipulates that the actual gum content of gasoline when it leaves the factory is not more than 5mg/100mL.
  • the actual gum of sec-butyl acetate is only 0.5-1.2 mg/lOOmL, which meets the requirements of the National III standard.
  • the doctoral test refers to the test of sodium sulfite and light petroleum products in the presence of sublimed sulfur to check the thiol or hydrogen sulfide in the oil, which can be determined according to the method specified in SH/T0174.
  • the principle of the doctoral test is: Put 10mL sample and 5mL sodium lead solution into a 50mL measuring cylinder with a grinding plug and shake vigorously. If the sample contains hydrogen sulfide, black lead sulfide is formed. If there is no such reaction, add a little pure and dry powdered sublimed sulfur and shake it again. If a thiol is present in the sample, a series of reactions will cause changes in the color of the oil layer and the sulfur film. Through testing, sec-butyl acetate was passed through a doctoral experiment.
  • Sulfur content refers to the content of sulfur and its derivatives (such as hydrogen sulfide, mercaptans, and disulfides, etc.) present in gasoline, expressed as a percentage by mass.
  • sulfur or sulfur derivatives contained in gasoline encounter water or water vapor, sulfurous acid and sulfuric acid are formed, which is more intense under the conditions of gasoline combustion. Sulfurous acid and sulfuric acid have a strong corrosive effect on metals.
  • sulfur can also reduce the octane number of gasoline and the sensitivity of gasoline to tetraethyl lead (ie, reduce the increase in the octane number of gasoline by adding tetraethyl lead). Therefore, the National III standard stipulates that the sulfur content should not exceed 150 ppm.
  • the sulfur content can be measured in accordance with the method specified in GB/T380.
  • the sulphur content of sec-butyl acetate is very low, below 3ppm, and is very suitable for the production of low-sulfur or even sulfur-free clean gasoline fuel. 17, methanol content
  • the production process of sec-butyl acetate does not produce methanol, and the raw material does not contain methanol. Therefore, the content of methanol in the sec-butyl acetate product is zero.
  • Benzene is a highly toxic chemical product.
  • the standard for benzene in motor gasoline is not more than 1.0% by volume.
  • the benzene content can be determined according to the method specified in SH/T0693. In the event of any objection to the determination of the benzene content, the results measured by the method specified in SH/T0713 shall prevail.
  • the sec-butyl acetate product was determined to be free of benzene.
  • Manganese content refers to the total manganese content in the form of methylcyclopentadienyl manganese tricarbonyl (MMT) in gasoline, and no other types of manganese-containing additives are added.
  • MMT methylcyclopentadienyl manganese tricarbonyl
  • the National III standard stipulates that the manganese content is not more than 0.016g/L and is determined by the method specified in SH/T0711.
  • the Beijing Standard C gasoline standard stipulates that the manganese content is not more than 0.006g/L.
  • the sec-butyl acetate product was determined to be free of manganese.
  • the sec-butyl acetate may be contained in an amount of from 1 to 30% by weight based on the total of the gasoline composition.
  • the content of sec-butyl acetate in the gasoline composition is less than 1% by weight, it is difficult to obtain a satisfactory effect of increasing the octane number and the antiknock index of the gasoline; when the content of sec-butyl acetate is high in the gasoline composition
  • the gasoline composition is corroded to the fuel filler pipe of the gas station and the rubber gasket in the fueling gun and the rubber fuel pipe of the gasoline engine.
  • the content of the sec-butyl acetate is preferably from the total amount of the gasoline composition from the viewpoint of further reducing the corrosiveness of various rubber articles in contact with the gasoline composition and controlling the oxygen content of the gasoline composition. 2-10% by weight.
  • the raw material gasoline in the gasoline composition according to the present invention may be various raw material gasolines which are commonly used in the art, and is not particularly limited.
  • the raw gasoline may be a commercially available finished gasoline that already contains various additives, such as: 90# gasoline, 93 # gasoline or 97 # gasoline; or gasoline fractions from refineries and chemical plants, for example: Catalytic cracking gasoline, alkylated gasoline, reformed gasoline, reformed raffinate oil, coking hydrogenated gasoline, straight run gasoline or light hydrocarbon C5, etc.
  • the light hydrocarbon C5 refers to various hydrocarbons having 5 carbon atoms and mixture.
  • the raw material gasoline in the gasoline composition of the present invention may further contain one or more of an ether compound, an alcohol compound, and an aromatic compound.
  • the total amount of the ether compound, the alcohol compound and the aromatic compound is 0.02 to 33% by weight based on the total amount of the gasoline composition.
  • the aromatic hydrocarbon compound may be various aromatic hydrocarbons commonly used in the art, and is not particularly limited.
  • the aromatic hydrocarbon compound is benzene, toluene, ethylbenzene, xylene (including ortho-xylene, meta-xylene and p-xylene), trimethylbenzene (including various isomers of trimethylbenzene), and C10 aromatic hydrocarbons.
  • the C10 aromatic hydrocarbon means an aromatic hydrocarbon having 10 carbon atoms and a mixture thereof.
  • the content of the aromatic hydrocarbon compound is preferably 0.02 to 33% by weight based on the total amount of the gasoline composition. From the viewpoint of environmental protection, the content of the benzene is preferably from 0.01 to 0.88% by weight based on the total amount of the gasoline composition.
  • the ether compound may be various ether compounds known to those skilled in the art.
  • the ether compound is one or more of methyl tert-butyl ether, ethyl tert-butyl ether, tert-amyl methyl ether and dibutyl ether.
  • the ether compound is contained in an amount of from 0.1 to 15% by weight based on the total of the gasoline composition.
  • the alcohol-based compound may be various alcohol-based compounds commonly used in the art.
  • the alcohol compound is one or more of methanol, ethanol, n-butanol, sec-butanol and tert-butanol.
  • the content of the alcohol compound is preferably 0.02 to 10% by weight.
  • the performance indexes of the gasoline composition according to the present invention are in compliance with the provisions of the National Standard for Automotive Gasoline III (GB17930-2006 (III)) (Table 2), which not only has a high octane number, but also is environmentally friendly. Table 2
  • the present invention also provides a method for preparing a gasoline composition, the method comprising the step of adding sec-butyl acetate to a raw gasoline, the amount of the sec-butyl acetate being added based on the total amount of the gasoline composition
  • the gasoline combination The content of sec-butyl acetate in the product is from 1 to 30% by weight, and the content of the raw gasoline is from 70 to 99% by weight.
  • the method for adding sec-butyl acetate to raw gasoline is not particularly limited, and may be various methods known to those skilled in the art as long as the raw gasoline can be uniformly mixed with sec-butyl acetate and sec-butyl acetate can be used.
  • the content can be within the specified range.
  • a predetermined amount of sec-butyl acetate may be slowly added to the raw gasoline in a mixer under stirring, and stirred uniformly; sec-butyl acetate and raw gasoline may be simultaneously added to the mixer and stirred. Evenly.
  • the method for producing a gasoline composition according to the present invention wherein the sec-butyl acetate is added in an amount such that the content of the sec-butyl acetate in the gasoline composition is 1 to 30% by weight based on the total amount of the gasoline composition. %.
  • the sec-butyl acetate is added in an amount such that the content of sec-butyl acetate in the gasoline composition is from 2 to 10% by weight based on the total amount of the gasoline composition.
  • the present invention has no particular limitation on the source of the sec-butyl acetate. Any commercially available sec-butyl acetate.
  • the purity of the sec-butyl acetate may be 80% by weight or more, preferably 90% by weight or more, and more preferably 97.5% by weight from the viewpoint of further reducing the content of the olefin in the gasoline composition and further increasing the octane number of the gasoline composition.
  • the above is particularly preferably 99% by weight or more.
  • the purity of the sec-butyl acetate is within the above range, the content of the olefin in the gasoline composition can be ensured to meet the requirements of the national standard III, and the octane number of the gasoline composition can meet the use requirements, and the gasoline can be lowered.
  • the cost of the composition is not limited to the above range.
  • the method further comprises the step of adding one or more of an ether compound, an alcohol compound and an aromatic compound to the raw gasoline.
  • the total amount of the ether compound, the alcohol compound, and the aromatic compound in the gasoline composition is 0.02 to 33% by weight based on the total amount of the gasoline composition.
  • the order of addition of the sec-butyl acetate, the ether compound, the alcohol compound, and the aromatic compound is not particularly limited, and one of an ether compound, an alcohol compound, and an aromatic compound is added to the raw gasoline.
  • the various steps and the step of adding sec-butyl acetate to the raw gasoline can achieve the objects of the present invention in various sequences.
  • the amount of the ether compound, the alcohol compound, and the aromatic compound to be added in the present invention is not particularly limited, and may be a conventional amount in the art as long as the gasoline composition is based on the total amount of the gasoline composition.
  • the total amount of the ether compound, the alcohol compound and the aromatic compound in the range is 0.02 to 33% by weight.
  • the ether compound is added in an amount such that the content of the ether compound in the gasoline composition is 0.1 to 15 by weight based on the total amount of the gasoline composition.
  • the alcohol-based compound is added in an amount such that the content of the alcohol-based compound in the gasoline composition is from 0.02 to 10% by weight
  • the aromatic hydrocarbon-based compound is added in an amount such that the aromatic hydrocarbon-based compound in the gasoline composition
  • the content is from 0.02 to 33% by weight.
  • the amount of benzene added to the aromatic compound to be added is such that the content of benzene in the gasoline composition is from 0.01 to 0.88% by weight based on the total amount of the gasoline composition.
  • Example 1 the test was carried out using the method specified in the Chinese National Standard GB17930-2006 (III).
  • Example 1 the test was carried out using the method specified in the Chinese National Standard GB17930-2006 (III).
  • This embodiment is intended to illustrate a gasoline composition and a method of producing the same according to the present invention.
  • sec-butyl acetate was purchased from Hunan Zhongchuang Chemical Co., Ltd. with a purity of 97.8 wt%, and the physical and chemical parameters of the sec-butyl acetate were as shown in Table 3 below.
  • This embodiment is intended to illustrate a gasoline composition and a method of producing the same according to the present invention.
  • This example employed the same raw material gasoline and sec-butyl acetate as in Example 1.
  • This embodiment is intended to illustrate a gasoline composition and a method of producing the same according to the present invention.
  • This example employed the same raw material gasoline and sec-butyl acetate as in Example 1.
  • This embodiment is intended to illustrate a gasoline composition and a method of producing the same according to the present invention.
  • This example employed the same raw material gasoline and sec-butyl acetate as in Example 1.
  • Example 2 The same raw material gasoline and sec-butyl acetate as in Example 1 were used.
  • Example 2 The same raw material gasoline and sec-butyl acetate as in Example 1 were used.
  • This embodiment is intended to illustrate a gasoline composition and a method of producing the same according to the present invention.
  • This example employs the same raw material gasoline as in the first embodiment.
  • Example 2 The same raw material gasoline as in Example 1 was used, and methyl tert-butyl ether having a purity of 98.5 wt% commercially available from Shanghai Yuanjing Chemical Co., Ltd. was used.
  • Example 2 The same raw material gasoline as in Example 1 was used, and n-butyl acetate having a purity of 98.5% by weight commercially available from Wuxi Baichuan Chemical Co., Ltd. was used.
  • Example 2 The same raw material gasoline as in Example 1 was used, and the purity of the commercially available product from Shanghai Maoji Chemical Reagent Co., Ltd. was
  • This embodiment is intended to illustrate a gasoline composition and a method of producing the same according to the present invention.
  • This example employs sec-butyl acetate which is commercially available from Hunan Zhongchuang Chemical Co., Ltd. with a purity of 80% by weight. 6.3 parts by weight of sec-butyl acetate was added to 93.7 parts by weight of raw gasoline (commercially available in #90 gasoline), and uniformly mixed to obtain a gasoline composition of the present invention, and the content of sec-butyl acetate in the gasoline composition was The technical specifications of the obtained gasoline composition containing sec-butyl acetate were 5% by weight as shown in Table 5 below.
  • This embodiment is intended to illustrate a gasoline composition and a method of producing the same according to the present invention.
  • This embodiment is intended to illustrate a gasoline composition and a method of producing the same according to the present invention.
  • Example 6 the same raw material gasoline as in Example 6 was used, and urethane butyl acetate having a purity of 97.5 wt% commercially available from Hunan Zhongchuang Chemical Co., Ltd. was used.
  • This embodiment is intended to illustrate a gasoline composition and a method of producing the same according to the present invention.
  • Example 6 the same raw material gasoline as in Example 6 was used, and urethane butyl acetate having a purity of 99% by weight commercially available from Hunan Zhongchuang Chemical Co., Ltd. was used.
  • This embodiment is intended to illustrate a gasoline composition and a method of producing the same according to the present invention.
  • sec-butyl acetate was purchased from Hunan Zhongchuang Chemical Co., Ltd. with a purity of 99.5% by weight.
  • the octane number and antiknock index of the sec-butyl acetate were as shown in Table 6 below. 8 parts by weight of sec-butyl acetate was added to 92 parts by weight of raw gasoline (light hydrocarbon C5 supplied by Zhonghai Shell Petrochemical Co., Ltd.), and uniformly mixed to obtain a gasoline composition of the present invention.
  • the content of the butyl ester was 8% by weight, and the octane number and the antiknock index of the obtained gasoline composition containing sec-butyl acetate were as shown in Table 6 below.
  • This embodiment is intended to illustrate a gasoline composition and a method of producing the same according to the present invention.
  • This example employs sec-butyl acetate having a purity of 80% by weight commercially available from Hunan Zhongchuang Chemical Co., Ltd., and the octane number and antiknock index of the sec-butyl acetate are shown in Table 6 below.
  • This embodiment is intended to illustrate a gasoline composition and a method of producing the same according to the present invention.
  • This example employs sec-butyl acetate having a purity of 90% by weight commercially available from Hunan Zhongchuang Chemical Co., Ltd., and the octane number and antiknock index of the sec-butyl acetate are shown in Table 6 below.
  • This embodiment is intended to illustrate a gasoline composition and a method of producing the same according to the present invention.
  • sec-butyl acetate having a purity of 95% by weight commercially available from Hunan Zhongchuang Chemical Co., Ltd. was used, and the octane number and antiknock index of the sec-butyl acetate were as shown in Table 6 below.
  • This embodiment is intended to illustrate a gasoline composition and a method of producing the same according to the present invention.
  • sec-butyl acetate having a purity of 95% by weight commercially available from Hunan Zhongchuang Chemical Co., Ltd. was used, and the physical and chemical parameters of the sec-butyl acetate were as shown in Table 7 below.
  • the gasoline composition of the present invention is obtained by mixing uniformly.
  • the content of the sec-butyl acetate in the obtained gasoline composition was 10% by weight, and the content of toluene was 10% by weight.
  • the technical parameters of the gasoline composition are shown in Table 7 below. Comparative example 6
  • a gasoline composition was prepared in the same manner as in Example 14, except that sec-butyl acetate was not added, and 20.5 parts by weight of toluene was added to 79.5 parts by weight of the raw material gasoline, and uniformly mixed to obtain a gasoline composition.
  • the technical parameters of the composition are shown in Table 7 below.
  • This embodiment is intended to illustrate a gasoline composition and a method of producing the same according to the present invention.
  • This example employed the same sec-butyl acetate and raw gasoline as in Example 14.
  • a gasoline composition was prepared in the same manner as in Example 15, except that sec-butyl acetate was not added, and 4.1 parts by weight of methyl t-butyl ether was added to 95.9 parts by weight of the raw gasoline, and the mixture was uniformly mixed to obtain a gasoline combination.
  • the technical parameters of the gasoline composition are shown in Table 7 below.
  • This embodiment is intended to illustrate a gasoline composition and a method of producing the same according to the present invention.
  • This example employed the same sec-butyl acetate and raw gasoline as in Example 14.
  • a gasoline composition was prepared in the same manner as in Example 16 except that 8.3 parts by weight of ethanol was added to 91.7 parts by weight of the raw material gasoline without adding sec-butyl acetate, and the mixture was uniformly mixed to obtain a gasoline composition.
  • the technical parameters of the composition are shown in Table 7 below.
  • This embodiment is intended to illustrate a gasoline composition and a method of producing the same according to the present invention.
  • the same sec-butyl acetate and raw gasoline were used as in Example 5.
  • a gasoline composition was prepared in the same manner as in Example 17, except that sec-butyl acetate was not added, and 10 parts by weight of ethyl t-butyl ether, 20 parts by weight of xylene, and 2 parts by weight of t-butyl, respectively.
  • the alcohol was separately added to 68 parts by weight of the raw material gasoline, and uniformly mixed to obtain a gasoline composition having a content of ethyl tert-butyl ether of 10% by weight and a content of xylene of 20% by weight, tert-butanol.
  • the content of the gasoline composition is as shown in Table 8 below.
  • This embodiment is intended to illustrate a gasoline composition and a method of producing the same according to the present invention.
  • a gasoline composition was prepared in the same manner as in Example 18 except that sec-butyl acetate was not added, and 6 parts by weight of methyl t-butyl ether and 10 parts by weight of xylene were separately added to 84 parts by weight of the raw materials.
  • a gasoline composition is obtained.
  • the content of methyl tert-butyl ether in the gasoline composition is 6% by weight, and the content of xylene is 10% by weight.
  • the technical parameters of the gasoline composition are as follows: 8 is shown. Table 8

Abstract

Disclosed are a gasoline composition and its preparation method. Said gasoline composition comprises raw gasoline and acetic acid secbutyl ester, in terms of the total weight of the gasoline composition, with the contents of acetic acid secbutyl ester being 1-30 weight%, contents of the raw gasoline being 70-99 weight%. The preparation method of the gasoline composition comprises the step of adding acetic acid secbutyl ester into raw gasoline.

Description

一种汽油组合物及其制备方法  Gasoline composition and preparation method thereof
技术领域 Technical field
本发明涉及一种汽油组合物及其制备方法,尤其涉及一种高辛烷值的汽油组合物及 其制备方法。 背景技术  The present invention relates to a gasoline composition and a process for the preparation thereof, and more particularly to a high octane gasoline composition and a process for the preparation thereof. Background technique
传统的提高汽油的辛烷值的添加组分主要是含铅化合物, 但由于含铅化合物对环境 的严重污染,中国已明令禁止生产含铅汽油。现今可以通过向汽油中添加芳烃类化合物、 含氧化合物或甲基环戊二烯三羰基锰 (MMT) 来提高汽油的辛烷值。  The traditional addition of octane in gasoline is mainly lead compounds, but due to the serious environmental pollution of lead compounds, China has banned the production of leaded gasoline. The octane number of gasoline can now be increased by adding an aromatic compound, an oxygenate or methylcyclopentadienyl manganese tricarbonyl (MMT) to the gasoline.
常用的含氧化合物主要包括醚系化合物和醇系化合物, 其中醚系化合物包括甲基叔 丁基醚 (MTBE)、 乙基叔丁基醚 (ETBE) 和叔戊基甲醚 (TAME)。 上述醚系化合物中 最常用的是 MTBE, 但 MTBE存在以下缺点: 一是 MTBE在水中的溶解度约为 4.2重 量%, 且 MTBE具有难闻的臭味, 在水中的含量超过 40-95pg/L时, 就会使水产生难闻 的气味; 二是 MTBE难于生物降解, 因而一旦掺有 MTBE的汽油泄漏, MTBE就将较 长期地残留在环境中。鉴于 MTBE容易对土壤和饮用水造成严重污染,在未来中国要实 施的城市清洁汽油标准中, 对 MTBE的加入量作了限制, 规定汽油中 MTBE的量不应 超过 15 重量%。 对于醇系化合物, 以甲醇、 乙醇和叔丁醇为主, 但醇系化合物的水溶 性很高, 遇水易与汽油分离, 对发动机性能造成负面影响, 因此醇系化合物的使用在一 定程度上受到了限制。 由于芳烃系化合物容易对环境造成负面影响, 因此, 芳烃系化合 物在汽油中的添加量也有严格的限制。  Commonly used oxygenates mainly include ether compounds and alcohol compounds, wherein the ether compounds include methyl tert-butyl ether (MTBE), ethyl tert-butyl ether (ETBE) and tert-amyl methyl ether (TAME). The most commonly used of the above ether compounds is MTBE, but MTBE has the following disadvantages: First, the solubility of MTBE in water is about 4.2% by weight, and MTBE has an unpleasant odor. When the content in water exceeds 40-95 pg/L. , it will make the water produce an unpleasant smell; Second, MTBE is difficult to biodegrade, so once the gasoline with MTBE is leaked, MTBE will remain in the environment for a longer period of time. In view of the fact that MTBE is likely to cause serious pollution to soil and drinking water, in the future urban clean gasoline standard to be implemented in China, the amount of MTBE added is limited, and the amount of MTBE in gasoline should not exceed 15% by weight. For the alcohol-based compound, methanol, ethanol and tert-butanol are the main ones, but the alcohol-based compound has high water solubility, and is easily separated from gasoline by water, which has a negative impact on engine performance. Therefore, the use of the alcohol-based compound is to some extent. Limited. Since the aromatic hydrocarbon compound is liable to have a negative impact on the environment, the amount of the aromatic hydrocarbon compound added to the gasoline is also severely limited.
此外, 甲基环戊二烯三羰基锰 (MMT) 也是目前国内比较常用的一种汽油添加剂。  In addition, methylcyclopentadienyl manganese tricarbonyl (MMT) is also a commonly used gasoline additive in China.
MMT是一种既能提高汽油辛烷值又不含铅的高效无铅汽油抗爆添加剂。 MMT的添加量 少且成本低, 因此受到广大用户的青睐。 但是 MMT的燃烧产物会在发动机的火花塞上 形成沉积物, 使燃烧条件变差; MMT见光易分解, 造成汽油使用过程中的辛烷值降低。 同时产生的含锰废气对环境造成严重污染, 现在大部分发达国家已经禁止使用 MMT。 中国现实行的中国国家第三阶段机动车排放标准(即, 国 III标准)也明确规定车用汽油 的锰含量不大于 0.016g/L。 MMT is a highly efficient unleaded gasoline antiknock additive that improves both octane and lead. MMT is less popular and less expensive, so it is favored by users. However, the combustion products of MMT will form deposits on the spark plug of the engine, which will deteriorate the combustion conditions; MMT will be easily decomposed by light, which will cause the octane number in the process of gasoline to decrease. At the same time, the manganese-containing waste gas generated serious pollution to the environment, and most developed countries have now banned the use of MMT. China's realistic third-stage motor vehicle emission standards (ie, National III standards) also clearly stipulate that the manganese content of motor gasoline is not more than 0.016g/L.
目前, 人们也开始关注酯系化合物作为提高汽油的辛烷值的添加组分的应用。  At present, attention has also been paid to the use of ester compounds as an additive component for increasing the octane number of gasoline.
CN1198466A公开了一种汽油添加剂组合物及其生产方法, 该汽油添加剂组合物是 由 0-5.0重量%的环戊二烯、 0.4-1.6重量%的卤代烯烃、 0-1.5重量%的卤代乙烷、 0.3-4.0 重量%的酯类、 30.0-65.0重量%的芳烃、 0-5.0重量%的酶、 1.0-5.0重量%的有机酸酐、 0-10.0重量%的蓖麻油、 30.00-60.0重量%的溶剂以及 0.001-0.02重量%的染料配制而成 的。 其中, 所述酯类的通式为 CxCOOCy (其中, X为 1-4的整数, y为 1-3的整数), 可 以为选自乙酸乙酯、 乙酸丙酯、 乙酸丁酯、 丙二酸二甲酯、 丙二酸二乙酯等中的一种或 两种的混合物, 其中, 两种酯的混合比例一般为 1 : 1-1: 3。 尽管该添加剂组合物可以 提高汽油的辛烷值, 但是, 该添加剂组合物中芳烃的含量很高, 因此, 汽油辛烷值的提 高实质上得益于添加的芳烃; 并且, 由于芳烃含量较高, 该添加剂组合物很难满足日益 严格的环保标准。 此外, 该汽油添加剂组合物的成分复杂, 配制工艺繁琐, 也不利于降 低成本。 CN1198466A discloses a gasoline additive composition and a method for producing the same, which comprises 0-5.0% by weight of cyclopentadiene, 0.4-1.6% by weight of halogenated olefin, 0-1.5% by weight of halogenated Ethane, 0.3-4.0% by weight of ester, 30.0-65.0% by weight of aromatic hydrocarbon, 0-5.0% by weight of enzyme, 1.0-5.0% by weight of organic acid anhydride, 0-10.0% by weight of castor oil, 30.00-60.0 by weight 5% solvent and 0.001-0.02% by weight dye. Wherein the ester has the formula C x COOC y (wherein X is an integer from 1 to 4, and y is an integer from 1 to 3), and may be selected from the group consisting of ethyl acetate, propyl acetate, and butyl acetate. A mixture of one or both of dimethyl malonate, diethyl malonate, and the like, wherein the mixing ratio of the two esters is generally 1:1:1:3. Although the additive composition can increase the octane number of the gasoline, the aromatic hydrocarbon content of the additive composition is high, and therefore, the increase in the octane number of the gasoline substantially benefits from the added aromatic hydrocarbon; and, because of the high aromatic content The additive composition is difficult to meet increasingly stringent environmental standards. In addition, the composition of the gasoline additive composition is complicated, the preparation process is cumbersome, and it is not conducive to lowering low cost.
CN1513954A公开了一种多功能燃料及其生产方法, 该多功能燃料的原料包括主体 原料和辅助原料两部分。 其中, 主体原料包括: 轻烃、 轻质油、 木精、磺化油、 煤焦油、 汽油和柴油; 辅助原料包括十八酸乙酯、 灰锰氧、 氢氧化钠、 水、 乙醇、 过氧化氢、 乙 萘酚、 石油醚、 环戊二烯铁、 丙酮、 甲苯、 植酸、 乙酸仲丁酯、 戊酸丁酯、 异戊烯、 醋 酸乙酯、 次氯酸钙、 四硼酸钠十水、 2-苯乙醇和环己酮。 上述辅料组成 A、 B、 C、 D四 组配方, 通过化学反应分别产生助溶剂、 增氧剂、 助燃剂、 消烟剂、 抗震防爆剂、 抗静 电剂、 防腐剂和烷值调节剂的作用。 其中, 各组配方的配比如下:  CN1513954A discloses a multifunctional fuel and a method for producing the same, the raw material of the multifunctional fuel comprising a main material and an auxiliary material. Among them, the main raw materials include: light hydrocarbons, light oil, wood essence, sulfonated oil, coal tar, gasoline and diesel; auxiliary materials including ethyl octadecanoate, ash manganese oxide, sodium hydroxide, water, ethanol, peroxidation Hydrogen, naphthol, petroleum ether, iron cyclopentadienide, acetone, toluene, phytic acid, sec-butyl acetate, butyl valerate, isoamylene, ethyl acetate, calcium hypochlorite, sodium tetraborate , 2-phenylethanol and cyclohexanone. The above auxiliary materials are composed of four groups of formulas A, B, C and D, which respectively produce a cosolvent, an oxygen enhancer, a combustion improver, a smoke suppressant, an anti-shock anti-vibration agent, an antistatic agent, a preservative and an alkane regulator. . Among them, the formula of each group of recipes is as follows:
A组:十八酸乙酯 2-20重量%,灰锰氧 3-15重量%,氢氧化钠 2-15重量%,水 40-80 重量%, 乙醇 5-30重量%;  Group A: ethyl octadecanoate 2-20% by weight, ash manganese oxide 3-15% by weight, sodium hydroxide 2-15% by weight, water 40-80% by weight, ethanol 5-30% by weight;
B组: 乙萘酚 5-25重量%, 石油醚 10-30重量%, 过氧化氢 5-20重量%, 环戊二烯 铁 5-30重量%, 丙酮 3-30重量%, 甲苯 5-30重量%;  Group B: 5-25 wt% of naphthol, 10-30 wt% of petroleum ether, 5-20 wt% of hydrogen peroxide, 5-30 wt% of iron cyclopentadiene, 3-30 wt% of acetone, toluene 5- 30% by weight;
C组: 植酸 5-25重量%, 乙酸仲丁酯 3-30重量%, 戊酸丁酯 5-30重量%, 异戊烯 10-40重量%, 醋酸乙酯 5-20重量%, 双氰胺 5-40重量%;  Group C: Phytic acid 5-25% by weight, sec-butyl acetate 3-30% by weight, butyl valerate 5-30% by weight, Isopenten 10-40% by weight, Ethyl acetate 5-20% by weight, Double Cyanamide 5-40% by weight;
D组: 联环己胺 2-20重量%, 次氯酸钙 3-30重量%, 四硼酸钠十水 5-35重量%, Group D: dicyclohexylamine 2-20% by weight, calcium hypochlorite 3-30% by weight, sodium tetraborate decahydrate 5-35 wt%,
2-苯乙醇 5-50重量%, 环己酮 5-30重量%, 多烯基丁二酰亚胺 5-35重量%。 2-phenylethanol 5-50% by weight, cyclohexanone 5-30% by weight, polyalkenyl succinimide 5-35 wt%.
由以上四组配方通过反应配制成综合添加剂 E组,然后根据需要将 E组添加到主料 中进行反应配制成多功能燃料。 该多功能燃料虽然用到了乙酸仲丁酯, 但乙酸仲丁酯仅 仅作为一种助剂而被添加到该多功能燃料中, 而且乙酸仲丁酯的添加量很低, 其中, 乙 酸仲丁酯在该多功能燃料中的添加量小于 0.5重量%。 并且, 尽管 CN1513954A还具体 公开了生产汽油发动机燃料时, 可以将 50重量份的 70号汽油、 30重量份的木精、 20 重量份的 120号溶剂油与 0.45份的 E组综合添加剂混合, 但并未公开制备的该汽油发 动机燃料的具体性能指标。  The above four groups of formulas are formulated into a comprehensive additive group E by reaction, and then the group E is added to the main material as needed to prepare a multifunctional fuel. Although the versatile fuel uses sec-butyl acetate, sec-butyl acetate is added to the multifunctional fuel as an auxiliary agent, and the amount of sec-butyl acetate added is low, wherein sec-butyl acetate The amount added in the multifunctional fuel is less than 0.5% by weight. Moreover, although CN1513954A specifically discloses the production of gasoline engine fuel, 50 parts by weight of No. 70 gasoline, 30 parts by weight of wood essence, 20 parts by weight of No. 120 solvent oil and 0.45 parts of Group E comprehensive additive may be mixed, but The specific performance specifications of the gasoline engine fuel prepared are not disclosed.
CN1513954A公开的燃油添加剂的主要问题在于: 燃料添加剂的成分多, 因此, 配 制工艺复杂, 成本过高; 以及 A、 B、 C、 D四组配方均含有烯烃类物质, 并且烯烃类物 质的含量均较高, 不利于降低汽油的烯烃含量, 因而不环保。  The main problem of the fuel additive disclosed in CN1513954A is that: the fuel additive has many components, and therefore, the preparation process is complicated and the cost is too high; and the four groups of formulas A, B, C and D contain olefins, and the content of olefins is Higher, it is not conducive to reducing the olefin content of gasoline, so it is not environmentally friendly.
EP0905217A公开了一种无铅汽油,该无铅汽油含有碳原子数为 2-15的含氧化合物, 所述含氧化合物在汽油中的含量使得以汽油的总量为基准,氧原子的含量为 0.1-15重量 %。 所述含氧化合物的引入可以降低发动机的排烟量, 抑制火花塞闷烧并减少汽油在燃 烧室中形成的积炭。 尽管 EP0905217A具体公开了所述含氧化合物可以为酯系化合物, 但是, 其实施例仅公开了分别含有甲基叔丁基醚、 叔戊基乙基醚和甲氧基丙基乙酸酯的 汽油, 并且公开的分别含有甲基叔丁基醚、 叔戊基乙基醚和甲氧基丙基乙酸酯的汽油的 辛烷值也没有显著的提高。  EP0905217A discloses an unleaded gasoline containing an oxygen-containing compound having 2 to 15 carbon atoms, the content of the oxygen-containing compound in gasoline being such that the content of oxygen atoms is based on the total amount of gasoline. 0.1-15% by weight. The introduction of the oxygenate can reduce the amount of smoke exhausted from the engine, suppress the smoldering of the spark plug, and reduce the build-up of gasoline in the combustion chamber. Although EP0905217A specifically discloses that the oxygenate may be an ester compound, the examples thereof only disclose gasoline containing methyl tert-butyl ether, tert-amylethyl ether and methoxypropyl acetate, respectively. And the disclosed octane number of gasoline containing methyl tert-butyl ether, tert-amylethyl ether and methoxypropyl acetate, respectively, was not significantly improved.
GB2114596A公开了一种燃料组合物,该燃料组合物含有 3-50体积%的乙酸叔丁酯; 并具体公开了含有 90体积%的汽油和 10体积%的乙酸叔丁酯的燃料组合物, 该燃料组 合物的研究法辛烷值和马达法辛烷值较原料汽油均有所提高, 但是, 乙酸叔丁酯作为一 种高档的化工中间品, 价格比较昂贵, 做为汽油的添加组分并不经济。  GB 2,114,596 A discloses a fuel composition comprising 3 to 50% by volume of t-butyl acetate; and specifically discloses a fuel composition comprising 90% by volume of gasoline and 10% by volume of t-butyl acetate. The octane number and motor octane number of the fuel composition are higher than that of the raw material gasoline. However, as a high-grade chemical intermediate, t-butyl acetate is relatively expensive and is added as a component of gasoline. uneconomic.
综上所述, 开发具有高的辛烷值、 长的诱导期、 低的胶质含量、 无毒害且价格低廉 的汽油添加剂, 从而环保、 高效地提高汽油的抗爆性正成为日益重要的研究课题。 发明内容 In summary, the development of gasoline additives with high octane number, long induction period, low gel content, non-toxic and low price, and environmentally friendly and efficient improvement of gasoline antiknock is becoming an increasingly important research. Question. Summary of the invention
本发明正是为了克服现有技术的不足,提供一种抗爆性好、诱导期长、胶质含量低、 绿色环保且成本低的汽油组合物及其制备方法, 该制备方法的操作简便且生产成本低。  The invention is to overcome the deficiencies of the prior art, and to provide a gasoline composition with good antiknocking property, long induction period, low gel content, green environmental protection and low cost, and a preparation method thereof, and the preparation method is simple and convenient to operate. Production costs are low.
根据本发明的汽油组合物含有原料汽油和乙酸仲丁酯, 且以所述汽油组合物的总量 计, 所述乙酸仲丁酯的含量为 1-30重量%, 所述原料汽油的含量为 70-99重量%。  The gasoline composition according to the present invention contains raw gasoline and sec-butyl acetate, and the content of the sec-butyl acetate is 1 to 30% by weight based on the total amount of the gasoline composition, and the content of the raw gasoline is 70-99% by weight.
根据本发明的汽油组合物的制备方法包括向原料汽油中添加乙酸仲丁酯的步骤, 以 所述汽油组合物的总量计,所述乙酸仲丁酯的添加量使得所述汽油组合物中的乙酸仲丁 酯的含量为 1-30重量%, 所述原料汽油的含量为 70-99重量%。  The method for producing a gasoline composition according to the present invention comprises the step of adding sec-butyl acetate to the raw gasoline, the amount of the sec-butyl acetate added in the gasoline composition based on the total amount of the gasoline composition The content of sec-butyl acetate is from 1 to 30% by weight, and the content of the raw gasoline is from 70 to 99% by weight.
本发明的汽油组合物采用乙酸仲丁酯作为添加剂 (即, 调和组分)。 与现有的汽油 添加剂相比, 特别是与用于改善汽油的抗爆性的添加剂相比, 乙酸仲丁酯的辛烷值高、 毒性小、 在水中的溶解性小且成本低, 因此, 乙酸仲丁酯是一种更为高效、 环保且经济 的汽油添加剂。  The gasoline composition of the present invention employs sec-butyl acetate as an additive (i.e., a blending component). Compared with existing gasoline additives, sec-butyl acetate has high octane number, low toxicity, low solubility in water and low cost, especially compared with additives for improving the antiknock property of gasoline. Secondary butyl acetate is a more efficient, environmentally friendly and economical gasoline additive.
根据本发明的汽油组合物, 所述汽油组合物中的乙酸仲丁酯能够提高现有汽油的辛 烷值和抗爆指数, 从而改善汽油的抗爆性。 同时, 所述汽油组合物中的乙酸仲丁酯还可 以起到稀释汽油组分中的芳烃含量的作用, 从而减轻芳烃对环境的污染。 并且, 含有乙 酸仲丁酯的汽油组合物不仅诱导期长,而且胶质含量低。此外, 乙酸仲丁酯的价格低廉, 不会附加提高汽油的成本。  According to the gasoline composition of the present invention, the sec-butyl acetate in the gasoline composition can improve the octane number and the antiknock index of the existing gasoline, thereby improving the antiknock property of the gasoline. At the same time, the sec-butyl acetate in the gasoline composition can also function to dilute the aromatics content of the gasoline component, thereby reducing the environmental pollution of the aromatic hydrocarbons. Further, the gasoline composition containing sec-butyl acetate has a long induction period and a low gel content. In addition, sec-butyl acetate is inexpensive and does not add to the cost of gasoline.
具体地, 通过在催化汽油中添加 9.8重量%的乙酸仲丁酯而得到的汽油组合物与作 为原料汽油的催化汽油相比, 研究法辛烷值由 90.4提高到 93.0, 马达法辛烷值由 81.4 提高到 83.6, 抗爆指数由 85.9提高到 88.3; 且含有 9.8重量%的乙酸仲丁酯的催化汽油 的诱导期大于 600分钟, 实际胶质含量仅为 2.77mg/100mL。  Specifically, the gasoline octane number of the gasoline composition obtained by adding 9.8% by weight of sec-butyl acetate to the catalytic gasoline is increased from 90.4 to 93.0, and the motor octane number is 81.4 increased to 83.6, the antiknock index increased from 85.9 to 88.3; and the induction period of catalytic gasoline containing 9.8% by weight of sec-butyl acetate was greater than 600 minutes, and the actual colloid content was only 2.77 mg/100 mL.
根据本发明的汽油组合物的制备方法, 对乙酸仲丁酯的纯度没有特别限制, 具有很 好的原料适应性。 并且, 根据本发明的汽油组合物的制备方法, 乙酸仲丁酯的使用方法 灵活, 不仅可以替代现有的汽油添加剂, 而且还可以与现有的汽油添加剂组合使用。 也 就是说, 本发明提供的汽油组合物的制备方法灵活, 可以通过在炼油厂或化工厂获得的 未经调和汽油的组分 (如催化汽油馏分、 直馏汽油馏分等) 中添加乙酸仲丁酯而获得, 也可以通过在现有成品汽油中添加乙酸仲丁酯而获得, 广谱性好, 能够全面改善在售成 品汽油和未经调和汽油的原料汽油的性能。  According to the method for producing a gasoline composition of the present invention, the purity of sec-butyl acetate is not particularly limited and has a good raw material suitability. Further, according to the method for producing a gasoline composition of the present invention, the use of sec-butyl acetate is flexible, and it can be used not only in place of the existing gasoline additive but also in combination with the existing gasoline additive. That is to say, the gasoline composition provided by the invention has a flexible preparation method, and can be added to the unreconciled gasoline component (such as catalytic gasoline fraction, straight-run gasoline fraction, etc.) obtained in a refinery or a chemical plant. Obtained from the ester, it can also be obtained by adding sec-butyl acetate to the existing finished gasoline, which has a broad spectrum and can comprehensively improve the performance of the raw gasoline in the finished gasoline and unconformed gasoline.
此外, 根据本发明的汽油组合物的制备方法操作简单, 无需加热和反应等复杂工艺 过程, 将乙酸仲丁酯添加到原料油中搅拌均匀即可。 具体实施方式  Further, the preparation method of the gasoline composition according to the present invention is simple in operation, and does not require a complicated process such as heating and reaction, and the sec-butyl acetate is added to the raw material oil and stirred uniformly. detailed description
根据本发明的汽油组合物含有原料汽油和乙酸仲丁酯, 且以所述汽油组合物的总量 计, 所述乙酸仲丁酯的含量为 1-30重量%, 所述原料汽油的含量为 70-99重量%。  The gasoline composition according to the present invention contains raw gasoline and sec-butyl acetate, and the content of the sec-butyl acetate is 1 to 30% by weight based on the total amount of the gasoline composition, and the content of the raw gasoline is 70-99% by weight.
乙酸仲丁酯是一种无色透明的液体, 不溶于水, 但可以溶于多数有机溶剂。 本发明 的发明人经过研究发现乙酸仲丁酯具有优异的综合性能, 是一种良好的汽油添加剂。 以 下结合相关性能指标进行详细描述。 1、 密度 Sec-butyl acetate is a colorless, transparent liquid that is insoluble in water but soluble in most organic solvents. The inventors of the present invention have found that sec-butyl acetate has excellent comprehensive properties and is a good gasoline additive. The following is a detailed description in conjunction with relevant performance indicators. 1, density
车用汽油的密度一般为 0.70-0.78kg/m3, 乙酸仲丁酯的密度为 0.862kg/m3, 在添加 量不大于 30重量%的条件下, 添加乙酸仲丁酯不会对车用汽油的密度造成不良影响。 The density of motor gasoline is generally 0.70-0.78kg/m 3 , the density of sec-butyl acetate is 0.862kg/m 3 , and the addition of sec-butyl acetate is not applicable to vehicles under the condition of not more than 30% by weight. The density of gasoline causes adverse effects.
2、 辛烷值和抗爆指数  2, octane number and anti-explosion index
辛烷值是衡量车用汽油抗爆性的一个重要的指标, 也是衡量汽油添加剂的一个重要 指标。  Octane number is an important indicator for measuring the antiknock resistance of motor gasoline. It is also an important indicator for measuring gasoline additives.
马达法辛烷值与研究法辛烷值 (辛烷值在 100或 100以下时) 都是在标准条件下, 把试样与已知辛烷值的参比燃料的爆震倾向进行比较。参比燃料是由异辛烷(辛烷值为 The motor octane number and the research octane number (when the octane number is below 100 or 100) are compared under standard conditions with the knocking tendency of the sample with a known octane reference fuel. The reference fuel is isooctane (octane number)
100 ) 和正庚烷 (辛烷值为零) 混合而成的, 与试样的爆震强度相当的参比燃料中所含 的异辛烷的体积百分数, 就是该试样的辛烷值。其中, 马达法辛烷值按 GB/T503的规定 进行测定, 研究法辛烷值按 GB/T5487的规定进行测定。 100) The volume percentage of isooctane contained in the reference fuel, which is a mixture of n-heptane (zero octane number) and equivalent to the knocking strength of the sample, is the octane number of the sample. Among them, the motor octane number is determined according to the provisions of GB/T503, and the research method octane number is determined according to the provisions of GB/T5487.
研究法辛烷值与马达法辛烷值的测定方法与和设备基本相同, 不同的只是测定时的 标准条件不同。 马达法辛烷值以较高的混合气温度 (一般加热至 149°C ) 和较高的发动 机转速 (900r/min ± 10r/min) 的苛刻条件为特征, 一般用以测定在发动机节气门全开和 发动机高速运转时汽油的抗爆性。而研究法辛烷值则以较低的混合气温度(一般不加热) 和较低的发动机转速 (600r/min ± 6r/min) 的中等苛刻条件为特征, 一般用以评定发动 机由低速过渡到中速运行时汽油的抗爆性。同一种汽油的研究法辛烷值一般要比马达法 辛烷值高, 可用下列关系式来近似换算两者的数值, 艮卩: The method for determining the octane number and the motor octane number is basically the same as that of the device, except that the standard conditions at the time of measurement are different. Motor octane is characterized by harsh conditions of higher gas mixture temperatures (typically heated to 149 ° C) and higher engine speeds (900 r/mi n ± 10 r /min), typically used to measure the throttle in the engine. The explosion resistance of gasoline when fully open and engine running at high speed. The research octane number is characterized by moderately harsh conditions of lower mixture temperature (generally not heated) and lower engine speed (600r/min ± 6r/min), which is generally used to assess the transition from low speed to The antiknock of gasoline at medium speed. The octane number of the same gasoline is generally higher than the motor octane number. The following relationship can be used to approximate the values of the two, 艮卩:
马达法辛烷值 =研究法辛烷值 X 0.8十 10。  Motor octane number = research method octane number X 0.8 ten 10.
研究法辛烷值与马达法辛烷值之差称为汽油的敏感性。  The difference between the octane number and the motor octane number is called the sensitivity of gasoline.
乙酸仲丁酯具有很高的辛烷值, 其中, 研究法辛烷值 (RON) 达到 119, 马达法辛 烷值 (MON) 达到 107, 明显高于常用的提高汽油的辛烷值的组分或添加剂 (表 1 )。  The sec-butyl acetate has a very high octane number, with a research octane number (RON) of 119 and a motor octane number (MON) of 107, which is significantly higher than the commonly used octane number of gasoline. Or additives (Table 1).
表 1  Table 1
Figure imgf000005_0001
马达法辛烷值与研究法辛烷值都是在专门的单缸发动机上, 在标准试验条件下测定 的, 很难全面反映车辆运行条件下燃料的抗爆性能。 因此, 提出了计算车辆实际运行条 件下的抗爆性能的经验关系, 艮
Figure imgf000005_0001
Both the motor octane number and the research octane number are measured on a dedicated single-cylinder engine under standard test conditions, and it is difficult to fully reflect the antiknock performance of the fuel under vehicle operating conditions. Therefore, the empirical relationship of calculating the antiknock performance under the actual operating conditions of the vehicle is proposed.
抗爆指数=(1€^十 MON)/2  Anti-explosion index = (1 € ^ ten MON) / 2
采用抗爆指数来反映一般运行条件下汽油的平均抗爆性能。 由上式可知, 汽油的辛 烷值越高, 它的抗爆性就越好, 发动机的动力性与经济性就越能得以体现。 乙酸仲丁酯 的抗爆指数为 113, 也明显高于表 1中列出的汽油添加剂的抗爆指数。  The antiknock index is used to reflect the average antiknock performance of gasoline under normal operating conditions. It can be seen from the above formula that the higher the octane number of gasoline, the better its explosion resistance, and the more the engine's power and economy can be reflected. The blast resistance index of sec-butyl acetate was 113, which was also significantly higher than the antiknock index of the gasoline additive listed in Table 1.
3、 馏程  3, distillation range
蒸发性是汽油最重要的特性之一。 汽油进入发动机气缸之前, 首先在气化室中迅速 气化并与空气形成可燃混合气。 一般情况下, 汽油在进气管中的停留时间只有Evaporation is one of the most important properties of gasoline. Before the gasoline enters the engine cylinder, it is first quickly in the gasification chamber. Gasifies and forms a combustible mixture with air. In general, the residence time of gasoline in the intake pipe is only
0.005-0.05S ,在汽缸内的蒸发时间也只有 0.02-0.03s。要在如此短的时间内形成均匀的可 燃混合气, 除了汽油机的构造和操作条件外, 更主要的因素是汽油本身的蒸发性。 反映 汽油的蒸发性能的指标是馏程和饱和蒸气压。 中国车用汽油的质量标准中, 馏程指标包 括 10体积%蒸发温度、 50体积%蒸发温度、 90体积%蒸发温度和终馏点 (δΡ, 干点)。 0.005-0.05S, the evaporation time in the cylinder is only 0.02-0.03s. In order to form a uniform combustible mixture in such a short period of time, in addition to the construction and operating conditions of the gasoline engine, the more important factor is the evaporability of the gasoline itself. The indicators reflecting the evaporation performance of gasoline are the distillation range and saturated vapor pressure. In the quality standards for Chinese motor gasoline, the distillation range indicators include 10% by volume evaporation temperature, 50% by volume evaporation temperature, 90% by volume evaporation temperature, and final boiling point (δΡ, dry point).
( 1 ) 10体积%蒸发温度  (1) 10% by volume evaporation temperature
10体积%蒸发温度表示汽油含有的低沸点馏分的多少,对汽油机启动的难易有决定 性影响, 同时, 也与产生气阻的倾向有密切的关系。 10体积%蒸发温度越低, 表明汽油 中所含有的低沸点馏分越多、 蒸发性越强, 使汽油机易于在低温下启动; 但是, 该蒸发 温度若过低, 则容易产生气阻。 中国车用汽油质量标准中要求 10体积%的蒸发温度不 高于 70°C。  The 10% by volume evaporation temperature indicates the amount of low-boiling fraction contained in gasoline, which has a decisive influence on the difficulty of starting the gasoline engine, and is also closely related to the tendency to generate gas resistance. The lower the 10% by volume evaporation temperature, the more low-boiling fractions contained in the gasoline and the higher the evaporability, making the gasoline engine easy to start at a low temperature; however, if the evaporation temperature is too low, gas resistance is likely to occur. China's motor gasoline quality standards require that 10% by volume of the evaporation temperature be no higher than 70 °C.
(2) 50体积%蒸发温度  (2) 50% by volume evaporation temperature
50体积%蒸发温度表示汽油的平均蒸发性能,与汽油机启动后升温时间的长短以及 加速是否及时均有密切关系。 汽油的 50体积%蒸发温度越低, 在正常温度下的蒸发量 也就越大, 从而能縮短汽油机的升温时间, 同时, 还可使发动机加速灵敏、 运转柔和。 如果 50体积%蒸发温度过高, 当发动机需要由低速转为高速、 供油量急剧增大时, 大 部分汽油不能气化, 导致燃烧不完全, 严重时甚至会突然熄火。 中国车用汽油质量标准 中要求 50体积%蒸发温度不高于 12CTC。  The 50% by volume evaporation temperature indicates the average evaporation performance of the gasoline, which is closely related to the length of the heating time after the gasoline engine is started and whether the acceleration is timely. The lower the 50% by volume evaporation temperature of gasoline, the greater the evaporation at normal temperature, which can shorten the heating time of the gasoline engine, and at the same time, make the engine more sensitive and softer. If the 50% by volume evaporation temperature is too high, when the engine needs to change from low speed to high speed and the fuel supply amount increases sharply, most of the gasoline cannot be vaporized, resulting in incomplete combustion, and even a sudden flameout in severe cases. China's motor gasoline quality standards require 50% evaporation temperature not higher than 12CTC.
(3) 90体积%蒸发温度和终馏点  (3) 90% by volume evaporation temperature and finishing point
90体积%蒸发温度和终馏点表示汽油中重质馏分含量的多少。 如果该温度过高, 说 明汽油中含有重质馏分过多, 不易保证汽油在使用条件下完全蒸发和完全燃烧。 这将导 致气缸积炭增多, 耗油率上升; 同时蒸发不完全的汽油重质馏分还会流入曲轴箱, 将润 滑油稀释从而加大磨损。中国车用汽油质量标准中要求 90体积%蒸发温度不高于 190°C, 终馏点不高于 205°C。  The 90% by volume evaporation temperature and the end point indicate the amount of heavy fraction in the gasoline. If the temperature is too high, it indicates that the gasoline contains too much heavy fraction, and it is not easy to ensure complete evaporation and complete combustion of the gasoline under the conditions of use. This will result in an increase in cylinder coke and an increase in fuel consumption. At the same time, the incompletely vaporized heavy fraction of gasoline will also flow into the crankcase, diluting the lubricating oil and increasing wear. In China's automotive gasoline quality standards, 90% of the evaporation temperature is not higher than 190 °C, and the final boiling point is not higher than 205 °C.
乙酸仲丁酯的沸点为 112.3°C, 并具有一定的挥发性, 添加到汽油中, 汽油的 10体 积%和 50体积%蒸发温度略有上升, 90体积%蒸发温度略有下降,不会对汽油组合物的 蒸发性能产生消极影响。  The sec-butyl acetate has a boiling point of 112.3 ° C and has a certain volatility. When added to gasoline, the evaporation temperature of 10% by volume and 50% by volume of gasoline slightly increases, and the evaporation temperature of 90% by volume decreases slightly. The evaporation performance of the gasoline composition has a negative impact.
4、 残留量  4, residual amount
汽油的残留量也是直接反应汽油品质的一个重要因素, 它表示汽油中最不易蒸发的 重质成分与储存过程中生成的氧化胶状物含量的多少。残留量指标高, 会使燃烧室及气 门组件积炭增加, 进气系统与化油器喉管结胶严重, 从而影响发动机的正常工作。 国 III 标准规定残留量不大于 2%。 乙酸仲丁酯基本无残留量, 不会对汽油组合物的残留量产 生消极影响。  The residual amount of gasoline is also an important factor in the direct response of gasoline quality. It represents the most difficult component of gasoline to evaporate and the amount of oxidized jelly produced during storage. The high residual index will increase the carbon deposits in the combustion chamber and valve components, and the intake system and the carburetor throat will be severely cemented, thus affecting the normal operation of the engine. The National III standard stipulates that the residual amount is not more than 2%. The sec-butyl acetate has substantially no residual amount and does not adversely affect the residual amount of the gasoline composition.
5、 饱和蒸气压  5, saturated vapor pressure
在规定条件下, 油品在适当的试验装置中, 气液两相达到平衡时, 液面蒸气所显示 的最大压力称为饱和蒸气压。饱和蒸气压用来评定汽油的蒸发强度, 是衡量汽油在汽油 机燃料供给系统中是否容易产生气阻的指标, 同时还可以衡量汽油在储存运输中的损耗 倾向。 汽油的饱和蒸气压越大, 蒸发性也就越强, 发动机易于冷启动, 但产生气阻的倾 向增大, 蒸发损耗也越大。 因此, 大气压力与环境温度不同时, 对汽油的饱和蒸气压的 要求也不同。国 III标准规定汽油蒸气压从 11月 1日至次年 4月 30日不大于 88kPa,从 5 月 1日至 10月 31 日不大于 72kPa。 Under the specified conditions, when the oil and gas are in equilibrium in a suitable test device, the maximum pressure displayed by the liquid surface vapor is called the saturated vapor pressure. Saturated vapor pressure is used to evaluate the evaporation strength of gasoline. It is a measure of whether gasoline is prone to generate gas resistance in a gasoline engine fuel supply system. It can also measure the loss tendency of gasoline in storage and transportation. The greater the saturated vapor pressure of gasoline, the stronger the evaporability, and the engine is prone to cold start, but the tendency to generate gas resistance increases, and the evaporation loss increases. Therefore, when the atmospheric pressure is different from the ambient temperature, the saturated vapor pressure of the gasoline The requirements are also different. The National III standard stipulates that the gasoline vapor pressure is not more than 88 kPa from November 1 to April 30, and is not more than 72 kPa from May 1 to October 31.
将乙酸仲丁酯添加到汽油中, 汽油的饱和蒸气压略有下降, 但影响较小, 完全可以 使含有乙酸仲丁酯的汽油符合中国国家标准。  When sec-butyl acetate is added to gasoline, the saturated vapor pressure of gasoline is slightly decreased, but the effect is small, and the gasoline containing sec-butyl acetate can meet the Chinese national standard.
6、 诱导期  6, induction period
诱导期指在规定的加速氧化条件下, 油品处于稳定状态所经历的时间周期, 可以按 照 GB/T8018 规定的方法进行测定。 方法概要为: 试样在氧弹中氧化, 此氧弹先在 15 °〇-25 下充氧至68§1^¾, 然后加热至 98 °C -102°C。 按规定的时间间隔读取压力、 或 连续记录压力, 直至到达转折点。 试样到达转折点所需要的时间即为试验温度下的实测 诱导期。 由此实测诱导期就可以计算 10CTC时的诱导期。汽油的诱导期以分钟计。显然, 汽油的诱导期长,则氧化和形成胶质的倾向就小。国 III标准规定汽油的诱导期不小于 480 分钟。 乙酸仲丁酯的诱导期大于 600分钟, 满足国 III的指标。 The induction period refers to the period of time that the oil is in a stable state under the specified accelerated oxidation conditions, and can be measured according to the method specified in GB/T8018. The method is summarized as follows: The sample is oxidized in an oxygen bomb. The oxygen bomb is first oxygenated at 65 ° 〇 -25 to 68 § 1^3⁄4 and then heated to 98 °C -102 °C. Read pressure at regular intervals, or continuously record pressure until the turning point is reached. The time required for the sample to reach the turning point is the measured induction period at the test temperature. From this measured induction period, the induction period at 10 CTC can be calculated. The induction period of gasoline is measured in minutes. Obviously, the induction period of gasoline is long, and the tendency to oxidize and form colloid is small. The National III standard stipulates that the induction period of gasoline is not less than 480 minutes. The induction period of sec-butyl acetate is greater than 600 minutes, meeting the national III index.
7、 水溶性酸或碱  7. Water-soluble acid or alkali
水溶性酸是指无机酸和低分子有机酸, 水溶性碱是指氢氧化钠等。 它们一般是在石 油炼制过程中残留下来的, 对金属有强烈的腐蚀作用, 汽油中不允许存在。 可以按照 GB/T259的规定测定汽油中水溶性酸或碱的含量。 方法概要为: 用蒸馏水或乙醇水溶液 抽提试样中的水溶性酸或碱, 然后, 分别用甲基橙或酚酞指示剂检查抽出液颜色的变化 情况, 或用酸度计测定抽提液的 pH值, 以判断有无水溶性酸或碱的存在。 乙酸仲丁酯 产品基本无水溶性酸, 也不含水溶性碱, 符合中国国家有关标准。  The water-soluble acid refers to a mineral acid and a low molecular organic acid, and the water-soluble alkali refers to sodium hydroxide or the like. They are generally left in the oil refining process and have a strong corrosive effect on metals. They are not allowed in gasoline. The content of water-soluble acid or alkali in gasoline can be determined in accordance with the provisions of GB/T259. The method outline is: extracting the water-soluble acid or alkali in the sample with distilled water or an aqueous solution of ethanol, and then checking the change of the color of the extract with methyl orange or phenolphthalein indicator, respectively, or determining the pH of the extract by using a pH meter Value to determine the presence or absence of a water soluble acid or base. The sec-butyl acetate product is basically free of water-soluble acid and water-soluble alkali, and conforms to relevant Chinese national standards.
8、 机械杂质及水  8, mechanical impurities and water
炼油厂炼制出的成品汽油是不含机械杂质与水分的, 但在储运及使用过程中, 汽油 不可避免地受到外界污染, 使得机械杂质及水分进入汽油中。 汽油中的机械杂质有可能 堵塞化油器量孔及汽油滤清器; 同时也会加剧化油器量孔、 气缸活塞组件的磨损。 汽油 中的水分在冬季则可能冻结, 严重时会堵塞滤清器或油路, 甚至造成供油中断; 另外, 水分还有加速机件腐蚀, 溶解抗氧剂, 加速汽油氧化生胶, 并引起四乙基铅分解, 使导 出剂等添加剂失效等不良作用。检查汽油中是否含有机械杂质及水分, 一般是将试样注 人 lOOmL的玻璃量筒中静置 8-12h后应当保持透明且没有悬浮和沉降的机械杂质及水 分。 在有异议时, 机械杂质可按 GB/T511规定的方法进行测定; 水分可按 GB/T260规 定的方法进行测定。 经实验测定, 乙酸仲丁酯中没有悬浮和沉降的机械杂质及水分。  The refined gasoline produced by the refinery does not contain mechanical impurities and moisture. However, during storage and use, the gasoline is inevitably polluted by the outside world, causing mechanical impurities and moisture to enter the gasoline. Mechanical impurities in the gasoline may block the carburetor orifice and the fuel filter; it also exacerbates the wear of the carburetor orifice and the cylinder piston assembly. The moisture in the gasoline may freeze in winter. In severe cases, it will block the filter or the oil circuit, and even cause the oil supply to be interrupted. In addition, the water also accelerates the corrosion of the parts, dissolves the antioxidants, accelerates the oxidation of the raw rubber, and causes Decomposition of tetraethyl lead causes undesirable effects such as failure of additives such as a propellant. Check the gasoline for mechanical impurities and moisture. Generally, the sample should be placed in a lOOmL glass cylinder for 8-12 hours and should remain transparent and free of suspended and settled mechanical impurities and moisture. In case of disagreement, the mechanical impurities can be measured according to the method specified in GB/T511; the moisture can be measured according to the method specified in GB/T260. There were no mechanical impurities and moisture suspended and settled in the sec-butyl acetate.
9、 芳烃含量  9, aromatic content
乙酸仲丁酯的生产工艺过程中无芳烃产生, 因此乙酸仲丁酯产品的芳烃含量为 0。 The production of sec-butyl acetate produces no aromatics, so the sec-butyl acetate product has an aromatic content of zero.
10、 烯烃含量 10, olefin content
车用汽油质量标准中规定, 烯烃的含量应当小于或等于 30 体积%。 尽管乙酸仲丁 酯的生产过程中有少量的烯烃类物质产生, 但是烯烃含量较低, 不会显著提高汽油的烯 烃含量。  The olefin content of motor gasoline should be less than or equal to 30% by volume. Although a small amount of olefins are produced during the production of sec-butyl acetate, the olefin content is low and does not significantly increase the olefin content of the gasoline.
11、 氧含量  11, oxygen content
限制车用汽油中的氧含量主要是考虑热值的问题, 汽油中氧含量增加, 则汽油中能 够燃烧的有效成分减少, 从而使热值降低, 影响发动机的动力。 另外, 汽油中氧含量过 高, 气缸中的积炭会越来越少, 气缸排气门失去积炭保护, 则磨损会更严重一些。 在现 行的车用汽油标准中, 汽油中的氧含量应当低于 2.7重量%。 尽管乙酸仲丁酯的含氧量 为 27.6重量%,但是通过控制乙酸仲丁酯在汽油中的添加量可以使含有乙酸仲丁酯的汽 油满足车用汽油标准的规定。 Limiting the oxygen content in motor gasoline is mainly a matter of considering the calorific value. When the oxygen content in the gasoline is increased, the effective component that can be burned in the gasoline is reduced, thereby lowering the calorific value and affecting the power of the engine. In addition, the oxygen content in gasoline has passed High, the carbon deposits in the cylinder will be less and less, and the cylinder exhaust valve loses the carbon deposit protection, so the wear will be more serious. In the current automotive gasoline standard, the oxygen content in gasoline should be less than 2.7% by weight. Although the oxygen content of sec-butyl acetate is 27.6% by weight, the gasoline containing sec-butyl acetate can satisfy the regulation of the gasoline standard for automobiles by controlling the amount of sec-butyl acetate added to the gasoline.
12、 铁含量  12, iron content
乙酸仲丁酯的生产过程中不使用铁制设备, 因此乙酸仲丁酯产品也不含铁。  Iron production equipment is not used in the production of sec-butyl acetate, so the sec-butyl acetate product is also free of iron.
13、 实际胶质  13, the actual gum
实际胶质一般用来说明汽油在进气管道及进气阀上可能生成沉积物的倾向, 是在规 定条件下测得的汽油蒸发残渣中的不溶于正庚烷的部分。 可以按照 GB/T8019的规定进 行测定, 方法概要为: 将已知量的燃料在控制温度和控制空气的条件下蒸发, 将正庚烷 抽提前和抽提后的残渣分别称重,所得结果以 mg/100mL报告,便可测得汽油实际胶质。 国 III标准规定汽油出厂时的实际胶质不大于 5mg/100mL。 乙酸仲丁酯的实际胶质仅为 0.5-1.2 mg/lOOmL, 满足国 III标准的规定。  The actual gum is generally used to illustrate the tendency of gasoline to form deposits on the intake pipe and the intake valve. It is the portion of the gasoline evaporation residue that is insoluble in n-heptane measured under specified conditions. It can be measured according to the provisions of GB/T8019. The method is summarized as follows: The known amount of fuel is evaporated under the conditions of controlled temperature and controlled air, and the residue after pre-heptane extraction and extraction is weighed separately, and the result is The mg/100mL report can be used to measure the actual gum quality of gasoline. The National III standard stipulates that the actual gum content of gasoline when it leaves the factory is not more than 5mg/100mL. The actual gum of sec-butyl acetate is only 0.5-1.2 mg/lOOmL, which meets the requirements of the National III standard.
14、 博士实验  14, doctoral experiment
博士试验是指在升华硫存在下, 用亚铅酸钠与轻质石油产品作用, 以检查油中的硫 醇或硫化氢的试验, 可以按照 SH/T0174规定的方法测定。 博士试验的方法原理是: 将 10mL试样与 5mL亚铅酸钠溶液放入带磨口塞的 50mL量筒内, 用力摇动。 如果试样含 硫化氢,则生成黑色的硫化铅。如无上述反应,则再加入少许纯净且干燥的粉状升华硫, 并再次摇动。 若试样中存在硫醇, 经过一系列反应, 会引起油层和硫膜颜色的变化。 通 过测试, 乙酸仲丁酯通过博士实验。  The doctoral test refers to the test of sodium sulfite and light petroleum products in the presence of sublimed sulfur to check the thiol or hydrogen sulfide in the oil, which can be determined according to the method specified in SH/T0174. The principle of the doctoral test is: Put 10mL sample and 5mL sodium lead solution into a 50mL measuring cylinder with a grinding plug and shake vigorously. If the sample contains hydrogen sulfide, black lead sulfide is formed. If there is no such reaction, add a little pure and dry powdered sublimed sulfur and shake it again. If a thiol is present in the sample, a series of reactions will cause changes in the color of the oil layer and the sulfur film. Through testing, sec-butyl acetate was passed through a doctoral experiment.
15、 铜片腐蚀 (50°C, 3h)  15. Copper corrosion (50°C, 3h)
在规定条件下测试油品对于铜的腐蚀趋向, 检查汽油中是否含有游离硫和活性硫化 物。 测定时, 按照 GB/T5096规定的方法进行, 方法概要为: 把一块已磨光的铜片浸没 在一定的试样中, 并按产品标准要求加热到指定的温度, 保持一定的时间。 待试验周期 结束时, 取出铜片, 经洗涤后与腐蚀标准色板进行比较, 确定腐蚀级别。 腐蚀标准色板 分为 4级, 其中: 1级为轻度变色; 2级为中度变色; 3级为深度变色; 4级为腐蚀。 国 III标准规定汽油的铜片腐蚀 (50°C, 3h) 不大于 1级。 乙酸仲丁酯的铜片腐蚀为 la, 符 合国 III标准的规定。  Test the corrosion tendency of the oil for copper under specified conditions and check if the gasoline contains free sulfur and active sulfur compounds. When measuring, according to the method specified in GB/T5096, the method is summarized as follows: A piece of polished copper piece is immersed in a certain sample and heated to the specified temperature according to the product standard for a certain period of time. At the end of the test period, the copper sheet is removed and compared to the corrosion standard swatch after washing to determine the corrosion level. Corrosion standard swatches are divided into 4 levels, of which: 1 is mild discoloration; 2 is moderate discoloration; 3 is deep discoloration; and 4 is corrosion. The National III standard stipulates that the corrosion of copper in gasoline (50 ° C, 3 h) is not greater than Class 1. The copper sheet of sec-butyl acetate is corroded to la, which meets the requirements of the National III standard.
16、 硫含量  16, sulfur content
硫含量是指存在于汽油中的硫及其衍生物(如硫化氢、硫醇和二硫化物等)的含量, 以质量百分比表示。汽油中含有的硫及硫的衍生物遇到水或水汽时, 会生成亚硫酸和硫 酸等,在汽油燃烧的条件下,这种趋向更为强烈。亚硫酸与硫酸对金属有强的腐蚀作用。 同时, 硫还能降低汽油的辛烷值及汽油对四乙基铅的感受性 (即, 减弱加入四乙基铅对 于汽油辛烷值的提高幅度)。 因此, 国 III标准规定硫含量不得大于 150ppm。 硫含量可以 按照 GB/T380规定的方法进行测定。  Sulfur content refers to the content of sulfur and its derivatives (such as hydrogen sulfide, mercaptans, and disulfides, etc.) present in gasoline, expressed as a percentage by mass. When sulfur or sulfur derivatives contained in gasoline encounter water or water vapor, sulfurous acid and sulfuric acid are formed, which is more intense under the conditions of gasoline combustion. Sulfurous acid and sulfuric acid have a strong corrosive effect on metals. At the same time, sulfur can also reduce the octane number of gasoline and the sensitivity of gasoline to tetraethyl lead (ie, reduce the increase in the octane number of gasoline by adding tetraethyl lead). Therefore, the National III standard stipulates that the sulfur content should not exceed 150 ppm. The sulfur content can be measured in accordance with the method specified in GB/T380.
乙酸仲丁酯的硫含量很低, 在 3ppm以下, 非常适合生产低硫甚至无硫的清洁汽油 燃料。 17、 甲醇含量 The sulphur content of sec-butyl acetate is very low, below 3ppm, and is very suitable for the production of low-sulfur or even sulfur-free clean gasoline fuel. 17, methanol content
乙酸仲丁酯的生产工艺过程不产生甲醇, 原料中也不含有甲醇, 因此, 乙酸仲丁酯 产品中甲醇的含量为 0。  The production process of sec-butyl acetate does not produce methanol, and the raw material does not contain methanol. Therefore, the content of methanol in the sec-butyl acetate product is zero.
18、 苯含量  18, benzene content
苯是一种毒害性较大的化工产品, 车用汽油标准规定苯含量不大于 1.0体积%, 苯 含量可以按照 SH/T0693规定的方法进行测定。在苯含量测定有异议时,以按照 SH/T0713 规定的方法测定的结果为准。 经测定, 乙酸仲丁酯产品不含苯。  Benzene is a highly toxic chemical product. The standard for benzene in motor gasoline is not more than 1.0% by volume. The benzene content can be determined according to the method specified in SH/T0693. In the event of any objection to the determination of the benzene content, the results measured by the method specified in SH/T0713 shall prevail. The sec-butyl acetate product was determined to be free of benzene.
19、 锰含量  19. Manganese content
锰含量是指汽油中以甲基环戊二烯三羰基锰 (MMT) 形式存在的总锰含量, 且不 得加入其他类型的含锰添加剂。 国 III标准规定, 锰含量不大于 0.016g/L, 采用 SH/T0711 规定的方法测定。 京标 C汽油标准中规定, 锰含量不大于 0.006g/L。 经测定, 乙酸仲丁 酯产品不含锰。  Manganese content refers to the total manganese content in the form of methylcyclopentadienyl manganese tricarbonyl (MMT) in gasoline, and no other types of manganese-containing additives are added. The National III standard stipulates that the manganese content is not more than 0.016g/L and is determined by the method specified in SH/T0711. The Beijing Standard C gasoline standard stipulates that the manganese content is not more than 0.006g/L. The sec-butyl acetate product was determined to be free of manganese.
上述分析结果表明, 乙酸仲丁酯的各项性能指标优异, 是一种优良的汽油添加剂。 根据本发明的汽油组合物, 以所述汽油组合物的总量计, 所述乙酸仲丁酯的含量可 以为 1-30重量%。 当汽油组合物中乙酸仲丁酯的含量低于 1重量%时, 很难获得令人满 意的提高汽油的辛烷值和抗爆指数的效果; 当汽油组合物中乙酸仲丁酯的含量高于 30 重量%时, 汽油组合物对加油站的加油管和加油枪中的橡胶垫圈以及汽油发动机的橡胶 导油管腐蚀增强。从进一步降低对与汽油组合物接触的各种橡胶制品的腐蚀性以及控制 汽油组合物的氧含量的角度出发, 以所述汽油组合物的总量计, 所述乙酸仲丁酯的含量 优选为 2-10重量%。  The above analysis results show that sec-butyl acetate has excellent performance indexes and is an excellent gasoline additive. According to the gasoline composition of the present invention, the sec-butyl acetate may be contained in an amount of from 1 to 30% by weight based on the total of the gasoline composition. When the content of sec-butyl acetate in the gasoline composition is less than 1% by weight, it is difficult to obtain a satisfactory effect of increasing the octane number and the antiknock index of the gasoline; when the content of sec-butyl acetate is high in the gasoline composition At 30% by weight, the gasoline composition is corroded to the fuel filler pipe of the gas station and the rubber gasket in the fueling gun and the rubber fuel pipe of the gasoline engine. The content of the sec-butyl acetate is preferably from the total amount of the gasoline composition from the viewpoint of further reducing the corrosiveness of various rubber articles in contact with the gasoline composition and controlling the oxygen content of the gasoline composition. 2-10% by weight.
根据本发明的汽油组合物中的原料汽油可以为本领域常用的各种原料汽油, 没有特 别的限定。具体地,所述原料汽油可以为市售的已经含有各种添加剂的成品汽油,例如: 90#汽油、 93 #汽油或 97 #汽油; 也可以为来自炼油厂和化工厂的汽油馏分, 例如: 催 化裂化汽油、 烷基化汽油、 重整汽油、 重整抽余油、 焦化加氢汽油、 直馏汽油或轻烃 C5等, 所述轻烃 C5指碳原子数为 5的各种烃及其混合物。  The raw material gasoline in the gasoline composition according to the present invention may be various raw material gasolines which are commonly used in the art, and is not particularly limited. Specifically, the raw gasoline may be a commercially available finished gasoline that already contains various additives, such as: 90# gasoline, 93 # gasoline or 97 # gasoline; or gasoline fractions from refineries and chemical plants, for example: Catalytic cracking gasoline, alkylated gasoline, reformed gasoline, reformed raffinate oil, coking hydrogenated gasoline, straight run gasoline or light hydrocarbon C5, etc., the light hydrocarbon C5 refers to various hydrocarbons having 5 carbon atoms and mixture.
本发明的汽油组合物中的原料汽油还可以含有醚系化合物、醇系化合物和芳烃系化 合物中的一种或多种。 以所述汽油组合物的总量计, 所述醚系化合物、 醇系化合物和芳 烃系化合物的总量为 0.02-33重量%。  The raw material gasoline in the gasoline composition of the present invention may further contain one or more of an ether compound, an alcohol compound, and an aromatic compound. The total amount of the ether compound, the alcohol compound and the aromatic compound is 0.02 to 33% by weight based on the total amount of the gasoline composition.
所述芳烃系化合物可以为本领域常用的各种芳香烃, 没有特别的限定。 优选地, 所 述芳烃系化合物为苯、 甲苯、 乙苯、 二甲苯 (包括邻二甲苯、 间二甲苯和对二甲苯)、 三甲苯 (包括三甲苯的各种异构体) 和 C10芳烃中的一种或多种。 所述 C10芳烃是指 碳原子数为 10的芳烃及其混合物。 以所述汽油组合物的总量计, 所述芳烃系化合物的 含量优选为 0.02-33重量%。 从环境保护的角度出发, 以所述汽油组合物的总量计, 所 述苯的含量优选为 0.01-0.88重量%。  The aromatic hydrocarbon compound may be various aromatic hydrocarbons commonly used in the art, and is not particularly limited. Preferably, the aromatic hydrocarbon compound is benzene, toluene, ethylbenzene, xylene (including ortho-xylene, meta-xylene and p-xylene), trimethylbenzene (including various isomers of trimethylbenzene), and C10 aromatic hydrocarbons. One or more. The C10 aromatic hydrocarbon means an aromatic hydrocarbon having 10 carbon atoms and a mixture thereof. The content of the aromatic hydrocarbon compound is preferably 0.02 to 33% by weight based on the total amount of the gasoline composition. From the viewpoint of environmental protection, the content of the benzene is preferably from 0.01 to 0.88% by weight based on the total amount of the gasoline composition.
所述醚系化合物可以为本领域技术人员公知的各种醚系化合物。 优选地, 所述醚系 化合物为甲基叔丁基醚、 乙基叔丁基醚、 叔戊基甲醚和丁醚中的一种或多种。 优选地, 以所述汽油组合物的总量计, 所述醚系化合物的含量为 0.1-15重量%。  The ether compound may be various ether compounds known to those skilled in the art. Preferably, the ether compound is one or more of methyl tert-butyl ether, ethyl tert-butyl ether, tert-amyl methyl ether and dibutyl ether. Preferably, the ether compound is contained in an amount of from 0.1 to 15% by weight based on the total of the gasoline composition.
所述醇系化合物可以为本领域常用的各种醇系化合物。 优选地, 所述醇系化合物为 甲醇、 乙醇、 正丁醇、 仲丁醇和叔丁醇中的一种或多种。 以所述汽油组合物的总量计, 所述醇系化合物的含量优选为 0.02-10重量%。 The alcohol-based compound may be various alcohol-based compounds commonly used in the art. Preferably, the alcohol compound is one or more of methanol, ethanol, n-butanol, sec-butanol and tert-butanol. Based on the total amount of the gasoline composition, The content of the alcohol compound is preferably 0.02 to 10% by weight.
根据本发明的汽油组合物的各项性能指标符合车用汽油国 III标准的规定 (GB17930-2006 (III)) (表 2), 不仅具有较高的辛烷值, 而且绿色环保。 表 2 The performance indexes of the gasoline composition according to the present invention are in compliance with the provisions of the National Standard for Automotive Gasoline III (GB17930-2006 (III)) (Table 2), which not only has a high octane number, but also is environmentally friendly. Table 2
Figure imgf000010_0001
本发明还提供了一种汽油组合物的制备方法, 该方法包括向原料汽油中添加乙酸仲 丁酯的步骤, 以所述汽油组合物的总量计, 所述乙酸仲丁酯的添加量使得所述汽油组合 物中的乙酸仲丁酯的含量为 1-30重量%, 所述原料汽油的含量为 70-99重量%。
Figure imgf000010_0001
The present invention also provides a method for preparing a gasoline composition, the method comprising the step of adding sec-butyl acetate to a raw gasoline, the amount of the sec-butyl acetate being added based on the total amount of the gasoline composition The gasoline combination The content of sec-butyl acetate in the product is from 1 to 30% by weight, and the content of the raw gasoline is from 70 to 99% by weight.
本发明对于向原料汽油中添加乙酸仲丁酯的方法并无特别限制, 可以为本领域技术 人员公知的各种方法,只要可以将原料汽油与乙酸仲丁酯混合均匀并使乙酸仲丁酯的含 量在规定范围内即可。 例如, 可以在混合器中, 在搅拌的条件下, 将预定量的乙酸仲丁 酯缓慢添加到原料汽油中并搅拌均匀; 也可以将乙酸仲丁酯和原料汽油同时添加到混合 器中并搅拌均匀。  The method for adding sec-butyl acetate to raw gasoline is not particularly limited, and may be various methods known to those skilled in the art as long as the raw gasoline can be uniformly mixed with sec-butyl acetate and sec-butyl acetate can be used. The content can be within the specified range. For example, a predetermined amount of sec-butyl acetate may be slowly added to the raw gasoline in a mixer under stirring, and stirred uniformly; sec-butyl acetate and raw gasoline may be simultaneously added to the mixer and stirred. Evenly.
根据本发明的汽油组合物的制备方法, 以所述汽油组合物的总量计, 所述乙酸仲丁 酯的添加量使得所述汽油组合物中的乙酸仲丁酯的含量为 1-30重量%。优选地, 以所述 汽油组合物的总量计,所述乙酸仲丁酯的添加量使得所述汽油组合物中的乙酸仲丁酯的 含量为 2-10重量%。  The method for producing a gasoline composition according to the present invention, wherein the sec-butyl acetate is added in an amount such that the content of the sec-butyl acetate in the gasoline composition is 1 to 30% by weight based on the total amount of the gasoline composition. %. Preferably, the sec-butyl acetate is added in an amount such that the content of sec-butyl acetate in the gasoline composition is from 2 to 10% by weight based on the total amount of the gasoline composition.
由于乙酸仲丁酯能够明显提高汽油的综合性能特别是辛烷值, 并且对乙酸仲丁酯本 身的纯度没有太高的要求, 因此本发明对于乙酸仲丁酯的来源并无特别的限制, 可以为 商购得到的任何乙酸仲丁酯。从进一步降低汽油组合物中烯烃的含量以及进一步提高汽 油组合物的辛烷值的角度出发, 乙酸仲丁酯的纯度可以为 80重量%以上, 优选为 90重 量%以上, 更优选为 97.5重量%以上, 特别优选为 99重量%以上。 当乙酸仲丁酯的纯度 处于上述范围之内时, 既能够保证汽油组合物中的烯烃的含量满足国 III标准的规定, 又能使汽油组合物的辛烷值满足使用要求, 还能够降低汽油组合物的成本。  Since the sec-butyl acetate can significantly improve the comprehensive performance of gasoline, especially the octane number, and the purity of the sec-butyl acetate itself is not too high, the present invention has no particular limitation on the source of the sec-butyl acetate. Any commercially available sec-butyl acetate. The purity of the sec-butyl acetate may be 80% by weight or more, preferably 90% by weight or more, and more preferably 97.5% by weight from the viewpoint of further reducing the content of the olefin in the gasoline composition and further increasing the octane number of the gasoline composition. The above is particularly preferably 99% by weight or more. When the purity of the sec-butyl acetate is within the above range, the content of the olefin in the gasoline composition can be ensured to meet the requirements of the national standard III, and the octane number of the gasoline composition can meet the use requirements, and the gasoline can be lowered. The cost of the composition.
根据本发明的汽油组合物的制备方法, 该方法还包括向原料汽油中添加醚系化合 物、 醇系化合物和芳烃系化合物中的一种或多种的步骤。 以所述汽油组合物的总量计, 所述汽油组合物中的所述醚系化合物、 醇系化合物和芳烃系化合物的总量为 0.02-33重 量%  According to the method for producing a gasoline composition of the present invention, the method further comprises the step of adding one or more of an ether compound, an alcohol compound and an aromatic compound to the raw gasoline. The total amount of the ether compound, the alcohol compound, and the aromatic compound in the gasoline composition is 0.02 to 33% by weight based on the total amount of the gasoline composition.
本发明对于乙酸仲丁酯、 醚系化合物、 醇系化合物和芳烃系化合物的添加顺序并无 特别限定, 所述向原料汽油中添加醚系化合物、 醇系化合物和芳烃系化合物中的一种或 多种的步骤和向原料汽油中添加乙酸仲丁酯的步骤采用各种顺序均能实现本发明的目 的。  In the present invention, the order of addition of the sec-butyl acetate, the ether compound, the alcohol compound, and the aromatic compound is not particularly limited, and one of an ether compound, an alcohol compound, and an aromatic compound is added to the raw gasoline. The various steps and the step of adding sec-butyl acetate to the raw gasoline can achieve the objects of the present invention in various sequences.
本发明对于所述醚系化合物、 醇系化合物和芳烃系化合物的添加量并无特别的限 定, 可以为本领域的常规用量, 只要以所述汽油组合物的总量计, 所述汽油组合物中的 所述醚系化合物、 醇系化合物和芳烃系化合物的总量为 0.02-33重量%。 但是从环保和 降低成本的角度出发, 优选地, 以所述汽油组合物的总量计, 所述醚系化合物的添加量 使得所述汽油组合物中的醚系化合物的含量为 0.1-15重量%, 所述醇系化合物的添加量 使得所述汽油组合物中的醇系化合物的含量为 0.02-10重量%, 所述芳烃系化合物的添 加量使得所述汽油组合物中的芳烃系化合物的含量为 0.02-33重量%。 从环境保护的角 度出发, 以所述汽油组合物的总量计, 所添加的芳烃系化合物中的苯的添加量使得所述 汽油组合物中苯的含量为 0.01-0.88重量%。  The amount of the ether compound, the alcohol compound, and the aromatic compound to be added in the present invention is not particularly limited, and may be a conventional amount in the art as long as the gasoline composition is based on the total amount of the gasoline composition. The total amount of the ether compound, the alcohol compound and the aromatic compound in the range is 0.02 to 33% by weight. However, from the viewpoint of environmental protection and cost reduction, preferably, the ether compound is added in an amount such that the content of the ether compound in the gasoline composition is 0.1 to 15 by weight based on the total amount of the gasoline composition. %, the alcohol-based compound is added in an amount such that the content of the alcohol-based compound in the gasoline composition is from 0.02 to 10% by weight, and the aromatic hydrocarbon-based compound is added in an amount such that the aromatic hydrocarbon-based compound in the gasoline composition The content is from 0.02 to 33% by weight. From the viewpoint of environmental protection, the amount of benzene added to the aromatic compound to be added is such that the content of benzene in the gasoline composition is from 0.01 to 0.88% by weight based on the total amount of the gasoline composition.
向所述汽油组合物中添加的所述醚系化合物、醇系化合物以及芳烃系化合物的种类 在前文已经进行了详细地描述, 此处不再赘述。  The types of the ether compound, the alcohol compound, and the aromatic compound added to the gasoline composition have been described in detail above and will not be described herein.
下面, 结合实施例对本发明进行更为详细地说明。  Hereinafter, the present invention will be described in more detail with reference to the embodiments.
以下实施例中, 采用中国国家标准 GB17930-2006 (III) 中规定的方法进行测试。 实施例 1 In the following examples, the test was carried out using the method specified in the Chinese National Standard GB17930-2006 (III). Example 1
本实施例用来说明根据本发明的汽油组合物及其制备方法。  This embodiment is intended to illustrate a gasoline composition and a method of producing the same according to the present invention.
本实施例采用商购自湖南中创化工股份有限公司的纯度为 97.8 重量%的乙酸仲丁 酯, 该乙酸仲丁酯的理化参数如下表 3所示。  In this example, sec-butyl acetate was purchased from Hunan Zhongchuang Chemical Co., Ltd. with a purity of 97.8 wt%, and the physical and chemical parameters of the sec-butyl acetate were as shown in Table 3 below.
将 2重量份的乙酸仲丁酯添加到 98重量份的原料汽油 (中石化长岭分公司提供的 催化裂化加氢汽油) 中, 混合均匀后得到本发明的汽油组合物, 该汽油组合物中乙酸仲 丁酯的含量为 2重量%, 得到的含有乙酸仲丁酯的汽油组合物的各项技术指标如下表 3 所示。 实施例 2  2 parts by weight of sec-butyl acetate was added to 98 parts by weight of raw gasoline (catalyzed cracked hydrogenated gasoline supplied by Sinopec Changling Branch), and uniformly mixed to obtain a gasoline composition of the present invention, and acetic acid in the gasoline composition The content of the sec-butyl ester was 2% by weight, and the technical specifications of the obtained gasoline composition containing sec-butyl acetate were as shown in Table 3 below. Example 2
本实施例用来说明根据本发明的汽油组合物及其制备方法。  This embodiment is intended to illustrate a gasoline composition and a method of producing the same according to the present invention.
本实施例采用与实施例 1相同的原料汽油和乙酸仲丁酯。  This example employed the same raw material gasoline and sec-butyl acetate as in Example 1.
将 5.1重量份的乙酸仲丁酯添加到 94.9重量份的原料汽油中 , 混合均匀后得到本发 明的汽油组合物, 该汽油组合物中乙酸仲丁酯的含量为 5重量%, 得到的含有乙酸仲丁 酯的汽油组合物的各项技术指标如下表 3所示。 实施例 3  5.1 parts by weight of sec-butyl acetate was added to 94.9 parts by weight of the raw gasoline, and after mixing, the gasoline composition of the present invention was obtained, and the content of the sec-butyl acetate in the gasoline composition was 5% by weight, and the obtained acetic acid was obtained. The technical specifications of the sec-butyl ester gasoline composition are shown in Table 3 below. Example 3
本实施例用来说明根据本发明的汽油组合物及其制备方法。  This embodiment is intended to illustrate a gasoline composition and a method of producing the same according to the present invention.
本实施例采用与实施例 1相同的原料汽油和乙酸仲丁酯。  This example employed the same raw material gasoline and sec-butyl acetate as in Example 1.
将 10重量份的乙酸仲丁酯添加到 90重量份的原料汽油中, 混合均匀后得到本发明 的汽油组合物, 该汽油组合物中乙酸仲丁酯的含量为 9.8重量%, 得到的含有乙酸仲丁 酯的汽油组合物的各项技术指标如下表 3所示。 实施例 4  10 parts by weight of sec-butyl acetate was added to 90 parts by weight of the raw material gasoline, and uniformly mixed to obtain a gasoline composition of the present invention, wherein the content of sec-butyl acetate in the gasoline composition was 9.8% by weight, and the obtained acetic acid was obtained. The technical specifications of the sec-butyl ester gasoline composition are shown in Table 3 below. Example 4
本实施例用来说明根据本发明的汽油组合物及其制备方法。  This embodiment is intended to illustrate a gasoline composition and a method of producing the same according to the present invention.
本实施例采用与实施例 1相同的原料汽油和乙酸仲丁酯。  This example employed the same raw material gasoline and sec-butyl acetate as in Example 1.
将 30.7重量份的乙酸仲丁酯添加到 69.3重量份的原料汽油中, 混合均匀后得到本 发明的汽油组合物, 该汽油组合物中乙酸仲丁酯的含量为 30 重量%, 得到的含有乙酸 仲丁酯的汽油组合物的各项技术指标如下表 3所示。  30.7 parts by weight of sec-butyl acetate was added to 69.3 parts by weight of the raw gasoline, and the mixture was uniformly mixed to obtain the gasoline composition of the present invention. The content of the sec-butyl acetate in the gasoline composition was 30% by weight, and the obtained acetic acid was obtained. The technical specifications of the sec-butyl ester gasoline composition are shown in Table 3 below.
对比例 1  Comparative example 1
采用与实施例 1相同的原料汽油和乙酸仲丁酯。  The same raw material gasoline and sec-butyl acetate as in Example 1 were used.
将 0.5重量份的乙酸仲丁酯添加到 99.5重量份的原料汽油中, 混合均匀后得到汽油 组合物, 该汽油组合物中乙酸仲丁酯的含量为 0.5重量%, 得到的含有乙酸仲丁酯的汽 油组合物的各项技术指标如下表 3所示。 对比例 2 0.5 parts by weight of sec-butyl acetate was added to 99.5 parts by weight of the raw gasoline, and after mixing, a gasoline composition was obtained, and the content of the sec-butyl acetate in the gasoline composition was 0.5% by weight, and the obtained sec-butyl acetate was obtained. The technical specifications of the gasoline composition are shown in Table 3 below. Comparative example 2
采用与实施例 1相同的原料汽油和乙酸仲丁酯。  The same raw material gasoline and sec-butyl acetate as in Example 1 were used.
将 35.8重量份的乙酸仲丁酯添加到 64.2重量份的原料汽油中, 混合均匀后得到汽 油组合物, 该汽油组合物中乙酸仲丁酯的含量为 35 重量%, 得到的含有乙酸仲丁酯的 汽油组合物的各项技术指标如下表 3所示。 表 3 35.8 parts by weight of sec-butyl acetate was added to 64.2 parts by weight of the raw gasoline, and after mixing, a gasoline composition was obtained, and the content of the sec-butyl acetate in the gasoline composition was 35 wt%, and the obtained sec-butyl acetate was obtained. The technical specifications of the gasoline composition are shown in Table 3 below. table 3
Figure imgf000013_0001
Figure imgf000013_0001
表 3的结果表明,含有 2-30重量%的乙酸仲丁酯的汽油组合物具有高的辛烷值和抗 爆指数。 实施例 5 The results in Table 3 indicate that the gasoline composition containing 2-30% by weight of sec-butyl acetate has a high octane number and an antiknock index. Example 5
本实施例用来说明根据本发明的汽油组合物及其制备方法。  This embodiment is intended to illustrate a gasoline composition and a method of producing the same according to the present invention.
本实施例采用与实施例 1相同的原料汽油。  This example employs the same raw material gasoline as in the first embodiment.
采用商购自湖南中创化工股份有限公司的纯度为 98.5重量%的乙酸仲丁酯,其各项 性能指标如下表 4所示;  The butyl urethane having a purity of 98.5% by weight, which is commercially available from Hunan Zhongchuang Chemical Co., Ltd., is shown in Table 4 below;
将 8.1重量份的乙酸仲丁酯添加到 91.9重量份的原料汽油中, 混合均匀后得到本发 明的汽油组合物, 该汽油组合物中乙酸仲丁酯的含量为 8重量%, 得到的含有乙酸仲丁 酯的汽油组合物的各项技术指标如下表 4所示。 对比例 3  8.1 parts by weight of sec-butyl acetate was added to 91.9 parts by weight of the raw gasoline, and the mixture was uniformly mixed to obtain the gasoline composition of the present invention. The content of the sec-butyl acetate in the gasoline composition was 8% by weight, and the obtained acetic acid was obtained. The technical specifications of the sec-butyl ester gasoline composition are shown in Table 4 below. Comparative example 3
采用与实施例 1 相同的原料汽油, 采用商购自上海源景化学品有限公司的纯度为 98.5重量%的甲基叔丁基醚。  The same raw material gasoline as in Example 1 was used, and methyl tert-butyl ether having a purity of 98.5 wt% commercially available from Shanghai Yuanjing Chemical Co., Ltd. was used.
将 8.1重量份的甲基叔丁基醚添加到 91.9重量份的原料汽油中, 混合均匀后得到含 有甲基叔丁基醚的汽油组合物, 该汽油组合物中甲基叔丁基醚的含量为 8重量%, 得到 的含有甲基叔丁基醚的汽油组合物的各项技术指标如下表 4所示。 对比例 4  8.1 parts by weight of methyl t-butyl ether was added to 91.9 parts by weight of the raw material gasoline, and uniformly mixed to obtain a gasoline composition containing methyl tert-butyl ether, and the content of methyl tert-butyl ether in the gasoline composition The technical specifications of the obtained gasoline composition containing methyl tert-butyl ether were 8% by weight as shown in Table 4 below. Comparative example 4
采用与实施例 1相同的原料汽油, 采用商购自无锡百川化工股份有限公司的纯度为 98.5重量%的乙酸正丁酯。  The same raw material gasoline as in Example 1 was used, and n-butyl acetate having a purity of 98.5% by weight commercially available from Wuxi Baichuan Chemical Co., Ltd. was used.
将 8.1重量份的乙酸正丁酯添加到 91.9重量份的原料汽油中, 混合均匀后得到含有 乙酸正丁酯的汽油组合物, 该汽油组合物中乙酸正丁酯的含量为 8重量%, 得到的含有 乙酸正丁酯的汽油组合物的各项技术指标如下表 4所示。 对比例 5  8.1 parts by weight of n-butyl acetate was added to 91.9 parts by weight of the raw material gasoline, and after mixing, a gasoline composition containing n-butyl acetate was obtained, and the content of n-butyl acetate in the gasoline composition was 8% by weight. The technical specifications of the gasoline composition containing n-butyl acetate are shown in Table 4 below. Comparative example 5
采用与实施例 1相同的原料汽油, 采用商购自上海茂基化学试剂有限公司的纯度为 The same raw material gasoline as in Example 1 was used, and the purity of the commercially available product from Shanghai Maoji Chemical Reagent Co., Ltd. was
98.5重量%的乙酸叔丁酯。 98.5 wt% t-butyl acetate.
将 8.1重量份的乙酸叔丁酯添加到 91.9重量份的原料汽油中, 混合均匀后得到含有 乙酸叔丁酯的汽油组合物, 该汽油组合物中乙酸叔丁酯的含量为 8重量%, 得到的含有 乙酸叔丁酯的汽油组合物的各项技术指标如下表 4所示。 表 4 8.1 parts by weight of t-butyl acetate was added to 91.9 parts by weight of the raw material gasoline, and after uniformly mixing, a gasoline composition containing t-butyl acetate was obtained, and the content of tert-butyl acetate in the gasoline composition was 8% by weight. The technical specifications of the gasoline composition containing t-butyl acetate are shown in Table 4 below. Table 4
Figure imgf000015_0001
表 4的结果表明, 与含有乙酸叔丁基醚的汽油组合物和含有乙酸正丁酯的汽油组合 物相比, 含有乙酸仲丁酯的汽油组合物具有更高的辛烷值和抗爆指数。 与含有乙酸叔丁 酯的汽油组合物相比, 含有乙酸仲丁酯的汽油组合物不仅实际胶质更少, 而且诱导期也 更长; 此外, 含有乙酸仲丁酯的汽油组合物的密度较含有乙酸叔丁酯的汽油组合物的密 度更低。 因此, 乙酸仲丁酯更适于用来调和汽油。 实施例 6
Figure imgf000015_0001
The results in Table 4 show that the gasoline composition containing sec-butyl acetate has a higher octane number and antiknock index than the gasoline composition containing t-butyl acetate and the gasoline composition containing n-butyl acetate. . Compared to gasoline compositions containing t-butyl acetate, gasoline compositions containing sec-butyl acetate have less actual gums and longer induction periods; in addition, the density of gasoline compositions containing sec-butyl acetate is higher. Gasoline compositions containing t-butyl acetate have a lower density. Therefore, sec-butyl acetate is more suitable for blending gasoline. Example 6
本实施例用来说明根据本发明的汽油组合物及其制备方法。  This embodiment is intended to illustrate a gasoline composition and a method of producing the same according to the present invention.
本实施例采用商购自湖南中创化工股份有限公司的纯度为 80重量%的乙酸仲丁酯。 将 6.3重量份的乙酸仲丁酯添加到 93.7重量份的原料汽油 (市售的 90#汽油) 中, 混合均匀后得到本发明的汽油组合物, 该汽油组合物中乙酸仲丁酯的含量为 5重量%, 得到的含有乙酸仲丁酯的汽油组合物的各项技术指标如下表 5所示。 实施例 7  This example employs sec-butyl acetate which is commercially available from Hunan Zhongchuang Chemical Co., Ltd. with a purity of 80% by weight. 6.3 parts by weight of sec-butyl acetate was added to 93.7 parts by weight of raw gasoline (commercially available in #90 gasoline), and uniformly mixed to obtain a gasoline composition of the present invention, and the content of sec-butyl acetate in the gasoline composition was The technical specifications of the obtained gasoline composition containing sec-butyl acetate were 5% by weight as shown in Table 5 below. Example 7
本实施例用来说明根据本发明的汽油组合物及其制备方法。  This embodiment is intended to illustrate a gasoline composition and a method of producing the same according to the present invention.
本实施例采用与实施例 6相同的原料汽油, 采用商购自湖南中创化工股份有限公司 的纯度为 90重量%的乙酸仲丁酯。  In this example, the same raw material gasoline as in Example 6 was used, and sec-butyl acetate was commercially available from Hunan Zhongchuang Chemical Co., Ltd. with a purity of 90% by weight.
将 5.6重量份的乙酸仲丁酯添加到 94.4重量份的原料汽油中, 混合均匀后得到本发 明的汽油组合物, 该汽油组合物中乙酸仲丁酯的含量为 5重量%, 得到的含有乙酸仲丁 酯的汽油组合物的各项技术指标如下表 5所示。 实施例 8  5.6 parts by weight of sec-butyl acetate was added to 94.4 parts by weight of the raw gasoline, and after mixing, the gasoline composition of the present invention was obtained, and the content of the sec-butyl acetate in the gasoline composition was 5% by weight, and the obtained acetic acid was obtained. The technical specifications of the sec-butyl ester gasoline composition are shown in Table 5 below. Example 8
本实施例用来说明根据本发明的汽油组合物及其制备方法。  This embodiment is intended to illustrate a gasoline composition and a method of producing the same according to the present invention.
本实施例采用与实施例 6相同的原料汽油, 采用商购自湖南中创化工股份有限公司 的纯度为 97.5重量%的乙酸仲丁酯。  In this example, the same raw material gasoline as in Example 6 was used, and urethane butyl acetate having a purity of 97.5 wt% commercially available from Hunan Zhongchuang Chemical Co., Ltd. was used.
将 5.1重量份的乙酸仲丁酯添加到 94.9重量份的原料汽油中, 混合均匀后得到本发 明的汽油组合物, 该汽油组合物中乙酸仲丁酯的含量为 5重量%, 得到的含有乙酸仲丁 酯的汽油组合物的各项技术指标如下表 5所示。 实施例 9  5.1 parts by weight of sec-butyl acetate was added to 94.9 parts by weight of the raw gasoline, and after mixing, the gasoline composition of the present invention was obtained, and the content of the sec-butyl acetate in the gasoline composition was 5% by weight, and the obtained acetic acid was obtained. The technical specifications of the sec-butyl ester gasoline composition are shown in Table 5 below. Example 9
本实施例用来说明根据本发明的汽油组合物及其制备方法。  This embodiment is intended to illustrate a gasoline composition and a method of producing the same according to the present invention.
本实施例采用与实施例 6相同的原料汽油, 采用商购自湖南中创化工股份有限公司 的纯度为 99重量%的乙酸仲丁酯。  In this example, the same raw material gasoline as in Example 6 was used, and urethane butyl acetate having a purity of 99% by weight commercially available from Hunan Zhongchuang Chemical Co., Ltd. was used.
将 5.1重量份的乙酸仲丁酯添加到 94.9重量份的原料汽油中, 混合均匀后得到本发 明的汽油组合物, 该汽油组合物中乙酸仲丁酯的含量为 5重量%, 得到的含有乙酸仲丁 酯的汽油组合物的各项技术指标如下表 5所示。 表 5 5.1 parts by weight of sec-butyl acetate was added to 94.9 parts by weight of the raw gasoline, and after mixing, the gasoline composition of the present invention was obtained, and the content of the sec-butyl acetate in the gasoline composition was 5% by weight, and the obtained acetic acid was obtained. The technical specifications of the sec-butyl ester gasoline composition are shown in Table 5 below. table 5
Figure imgf000017_0001
表 5的结果表明, 根据本发明的制备汽油组合物的方法对于乙酸仲丁酯的纯度等级 没有特别的限定, 纯度等级不低于 80重量%的乙酸仲丁酯均可使用, 因此根据本发明 的制备汽油组合物的方法的原料适应性好。 实施例 10
Figure imgf000017_0001
The results of Table 5 show that the method for producing a gasoline composition according to the present invention has no particular limitation on the purity level of sec-butyl acetate, and sec-butyl acetate having a purity level of not less than 80% by weight can be used, and thus according to the present invention The method for preparing a gasoline composition has good material adaptability. Example 10
本实施例用来说明根据本发明的汽油组合物及其制备方法。  This embodiment is intended to illustrate a gasoline composition and a method of producing the same according to the present invention.
本实施例采用商购自湖南中创化工股份有限公司的纯度为 99.5 重量%的乙酸仲丁 酯, 该乙酸仲丁酯的辛烷值和抗爆指数如下表 6所示。 将 8重量份的乙酸仲丁酯添加到 92重量份的原料汽油 (中海壳牌石油化工有限公 司提供的轻烃 C5 ) 中, 混合均匀后得到本发明的汽油组合物, 该汽油组合物中乙酸仲 丁酯的含量为 8重量%, 得到的含有乙酸仲丁酯的汽油组合物的辛烷值和抗爆指数如下 表 6所示。 实施例 11 In this example, sec-butyl acetate was purchased from Hunan Zhongchuang Chemical Co., Ltd. with a purity of 99.5% by weight. The octane number and antiknock index of the sec-butyl acetate were as shown in Table 6 below. 8 parts by weight of sec-butyl acetate was added to 92 parts by weight of raw gasoline (light hydrocarbon C5 supplied by Zhonghai Shell Petrochemical Co., Ltd.), and uniformly mixed to obtain a gasoline composition of the present invention. The content of the butyl ester was 8% by weight, and the octane number and the antiknock index of the obtained gasoline composition containing sec-butyl acetate were as shown in Table 6 below. Example 11
本实施例用来说明根据本发明的汽油组合物及其制备方法。  This embodiment is intended to illustrate a gasoline composition and a method of producing the same according to the present invention.
本实施例采用商购自湖南中创化工股份有限公司的纯度为 80重量%的乙酸仲丁酯, 该乙酸仲丁酯的辛烷值和抗爆指数如下表 6所示。  This example employs sec-butyl acetate having a purity of 80% by weight commercially available from Hunan Zhongchuang Chemical Co., Ltd., and the octane number and antiknock index of the sec-butyl acetate are shown in Table 6 below.
将 37.5重量份的乙酸仲丁酯添加到 62.5重量份的原料汽油 (中石化长岭分公司提 供的直馏汽油) 中, 混合均匀后得到本发明的汽油组合物, 该汽油组合物中乙酸仲丁酯 的含量为 30重量%,得到的含有乙酸仲丁酯的汽油组合物的辛烷值和抗爆指数如下表 6 所示。 实施例 12  37.5 parts by weight of sec-butyl acetate was added to 62.5 parts by weight of raw gasoline (straight-run gasoline provided by Sinopec Changling Branch), and uniformly mixed to obtain the gasoline composition of the present invention, and the gasoline composition was sec-butyl acetate. The content of the ester was 30% by weight, and the octane number and the antiknock index of the obtained gasoline composition containing sec-butyl acetate were as shown in Table 6 below. Example 12
本实施例用来说明根据本发明的汽油组合物及其制备方法。  This embodiment is intended to illustrate a gasoline composition and a method of producing the same according to the present invention.
本实施例采用商购自湖南中创化工股份有限公司的纯度为 90重量%的乙酸仲丁酯, 该乙酸仲丁酯的辛烷值和抗爆指数如下表 6所示。  This example employs sec-butyl acetate having a purity of 90% by weight commercially available from Hunan Zhongchuang Chemical Co., Ltd., and the octane number and antiknock index of the sec-butyl acetate are shown in Table 6 below.
将 16.7重量份的乙酸仲丁酯添加到 83.3重量份的原料汽油 (中石化上海分公司提 供的重整抽余油) 中, 混合均匀后得到本发明的汽油组合物, 该汽油组合物中乙酸仲丁 酯的含量为 15 重量%, 得到的含有乙酸仲丁酯的汽油组合物的辛烷值和抗爆指数如下 表 6所示。 实施例 13  16.7 parts by weight of sec-butyl acetate was added to 83.3 parts by weight of raw gasoline (reconstituted raffinate oil supplied by Sinopec Shanghai Branch), and uniformly mixed to obtain a gasoline composition of the present invention. The content of the butyl ester was 15% by weight, and the octane number and the antiknock index of the obtained gasoline composition containing sec-butyl acetate were as shown in Table 6 below. Example 13
本实施例用来说明根据本发明的汽油组合物及其制备方法。  This embodiment is intended to illustrate a gasoline composition and a method of producing the same according to the present invention.
本实施例采用商购自湖南中创化工股份有限公司的纯度为 95重量%的乙酸仲丁酯, 该乙酸仲丁酯的辛烷值和抗爆指数如下表 6所示。  In this example, sec-butyl acetate having a purity of 95% by weight commercially available from Hunan Zhongchuang Chemical Co., Ltd. was used, and the octane number and antiknock index of the sec-butyl acetate were as shown in Table 6 below.
将 2.1重量份的乙酸仲丁酯添加到 97.9重量份的原料汽油(中石化长岭分公司提供 的重整汽油) 中, 混合均匀后得到本发明的汽油组合物, 该汽油组合物中乙酸仲丁酯的 含量为 2重量%, 得到的含有乙酸仲丁酯的汽油组合物的辛烷值和抗爆指数如下表 6所 示。 表 6 2.1 parts by weight of sec-butyl acetate was added to 97.9 parts by weight of raw gasoline (reformed gasoline supplied by Sinopec Changling Branch), and uniformly mixed to obtain a gasoline composition of the present invention, and the gasoline composition was sec-butyl acetate. The content of the ester was 2% by weight, and the octane number and the antiknock index of the obtained gasoline composition containing sec-butyl acetate were as shown in Table 6 below. Table 6
Figure imgf000019_0001
表 6的结果表明, 根据本发明的制备汽油组合物的方法可以用于提高各种来源的原 料汽油的辛烷值, 广谱性好。 实施例 14
Figure imgf000019_0001
The results of Table 6 show that the method for preparing a gasoline composition according to the present invention can be used to increase the octane number of raw material gasoline of various sources, and has a broad spectrum. Example 14
本实施例用来说明根据本发明的汽油组合物及其制备方法。  This embodiment is intended to illustrate a gasoline composition and a method of producing the same according to the present invention.
本实施例采用商购自湖南中创化工股份有限公司的纯度为 95重量%的乙酸仲丁酯, 该乙酸仲丁酯的理化参数如下表 7所示。  In this example, sec-butyl acetate having a purity of 95% by weight commercially available from Hunan Zhongchuang Chemical Co., Ltd. was used, and the physical and chemical parameters of the sec-butyl acetate were as shown in Table 7 below.
将 10.5重量份的乙酸仲丁酯和 10重量份的甲苯 (商购自中石化长岭炼厂,纯度 98.5 重量%)分别添加到 79.5重量份的原料汽油(商购自中石化长岭分公司的催化裂化加氢 汽油) 中, 混合均匀后得到本发明的汽油组合物。 得到的汽油组合物中的乙酸仲丁酯的 含量为 10重量%, 甲苯的含量为 10重量%, 该汽油组合物的各项技术指标参数如下表 7所示。 对比例 6  Adding 10.5 parts by weight of sec-butyl acetate and 10 parts by weight of toluene (commercially available from Sinopec Changling Refinery, purity 98.5 wt%) to 79.5 parts by weight of raw gasoline (commercially available from Sinopec Changling Branch) In the cracked hydrogenated gasoline, the gasoline composition of the present invention is obtained by mixing uniformly. The content of the sec-butyl acetate in the obtained gasoline composition was 10% by weight, and the content of toluene was 10% by weight. The technical parameters of the gasoline composition are shown in Table 7 below. Comparative example 6
采用与实施例 14相同的方法制备汽油组合物, 不同的是, 不添加乙酸仲丁酯, 将 20.5重量份的甲苯添加到 79.5重量份的原料汽油中,混合均匀后得到汽油组合物,该汽 油组合物的各项技术指标参数如下表 7所示。 实施例 15  A gasoline composition was prepared in the same manner as in Example 14, except that sec-butyl acetate was not added, and 20.5 parts by weight of toluene was added to 79.5 parts by weight of the raw material gasoline, and uniformly mixed to obtain a gasoline composition. The technical parameters of the composition are shown in Table 7 below. Example 15
本实施例用来说明根据本发明的汽油组合物及其制备方法。  This embodiment is intended to illustrate a gasoline composition and a method of producing the same according to the present invention.
本实施例采用与实施例 14相同的乙酸仲丁酯和原料汽油。  This example employed the same sec-butyl acetate and raw gasoline as in Example 14.
将 2.1重量份的乙酸仲丁酯和 2重量份的甲基叔丁基醚 (商购自上海源景化学品有 限公司, 纯度为 98.5重量%) 添加到 95.9重量份原料汽油中, 混合均匀后得到本发明 的汽油组合物。 得到的汽油组合物中的乙酸仲丁酯的含量为 2重量%, 甲基叔丁基醚的 含量为 2重量%, 该汽油组合物的各项技术指标如下表 7所示。 对比例 7 2.1 parts by weight of sec-butyl acetate and 2 parts by weight of methyl t-butyl ether (commercially available from Shanghai Yuanjing Chemical Co., Ltd., purity of 98.5 wt%) were added to 95.9 parts by weight of raw gasoline, and after mixing uniformly The gasoline composition of the present invention is obtained. The content of sec-butyl acetate in the obtained gasoline composition was 2% by weight, and the content of methyl tert-butyl ether was 2% by weight. The technical specifications of the gasoline composition are shown in Table 7 below. Comparative example 7
采用与实施例 15相同的方法制备汽油组合物, 不同的是, 不添加乙酸仲丁酯, 将 4.1重量份的甲基叔丁基醚添加到 95.9重量份原料汽油中,混合均匀后得到汽油组合物, 该汽油组合物的各项技术指标参数如下表 7所示。 实施例 16  A gasoline composition was prepared in the same manner as in Example 15, except that sec-butyl acetate was not added, and 4.1 parts by weight of methyl t-butyl ether was added to 95.9 parts by weight of the raw gasoline, and the mixture was uniformly mixed to obtain a gasoline combination. The technical parameters of the gasoline composition are shown in Table 7 below. Example 16
本实施例用来说明根据本发明的汽油组合物及其制备方法。  This embodiment is intended to illustrate a gasoline composition and a method of producing the same according to the present invention.
本实施例采用与实施例 14相同的乙酸仲丁酯和原料汽油。  This example employed the same sec-butyl acetate and raw gasoline as in Example 14.
将 5.3重量份的乙酸仲丁酯和 3重量份的乙醇(商购自河南天冠燃料乙醇有限公司, 纯度为 98.5重量%) 添加到 91.7重量份的原料汽油中, 混合均匀后得到本发明的汽油 组合物。得到的汽油组合物中的乙酸仲丁酯的含量为 5重量%, 乙醇的含量为 3重量%, 该汽油组合物的各项技术指标如下表 7所示。 对比例 8  5.3 parts by weight of sec-butyl acetate and 3 parts by weight of ethanol (commercially available from Henan Tianguan Fuel Ethanol Co., Ltd., purity of 98.5 wt%) were added to 91.7 parts by weight of raw gasoline, and uniformly mixed to obtain the present invention. Gasoline composition. The content of sec-butyl acetate in the obtained gasoline composition was 5% by weight, and the content of ethanol was 3% by weight. The technical specifications of the gasoline composition are shown in Table 7 below. Comparative example 8
采用与实施例 16相同的方法制备汽油组合物 , 不同的是, 不添加乙酸仲丁酯, 将 8.3重量份的乙醇添加到 91.7重量份的原料汽油中, 混合均匀后得到汽油组合物, 该汽 油组合物的各项技术指标参数如下表 7所示。 A gasoline composition was prepared in the same manner as in Example 16 except that 8.3 parts by weight of ethanol was added to 91.7 parts by weight of the raw material gasoline without adding sec-butyl acetate, and the mixture was uniformly mixed to obtain a gasoline composition. The technical parameters of the composition are shown in Table 7 below.
表 7 Table 7
Figure imgf000021_0001
表 7的结果表明, 乙酸仲丁酯可以与其它汽油添加剂组合使用。 将实施例 14与对 比例 6对比可以看出, 乙酸仲丁酯不仅可以用来提高汽油的辛烷值和抗爆指数, 而且还 可以稀释汽油中的芳烃含量。 将实施例 15与对比例 7、 实施例 16与对比例 8对比可以 看出, 在添加量相同的条件下, 含有乙酸仲丁酯的汽油组合物具有更高的辛烷值和抗爆 指数。 实施例 17
Figure imgf000021_0001
The results in Table 7 indicate that sec-butyl acetate can be used in combination with other gasoline additives. Comparing Example 14 with Comparative Example 6, it can be seen that sec-butyl acetate can be used not only to increase the octane number and the antiknock index of gasoline, but also to dilute the aromatic content in gasoline. Comparing Example 15 with Comparative Example 7, Example 16 and Comparative Example 8, it can be seen that the gasoline composition containing sec-butyl acetate has a higher octane number and antiknock index under the same conditions of addition. Example 17
本实施例用来说明根据本发明的汽油组合物及其制备方法。 采用与实施例 5相同的乙酸仲丁酯和原料汽油。 This embodiment is intended to illustrate a gasoline composition and a method of producing the same according to the present invention. The same sec-butyl acetate and raw gasoline were used as in Example 5.
将 5重量份的乙酸仲丁酯、 5重量份的乙基叔丁基醚 (商购自广州伟伯化工有限公 司, 纯度为 98.5重量%)、 20重量份的二甲苯(商购自中石化长岭炼厂, 纯度为 98.5重 量%) 和 2重量份的叔丁醇 (商购自上海新高化学试剂有限公司, 纯度为 98.5重量%) 分别添加到 68重量份的原料汽油中, 混合均匀后得到本发明的汽油组合物, 该汽油组 合物中乙酸仲丁酯的含量为 5重量%, 乙基叔丁基醚的含量为 5重量%, 二甲苯的含量 为 20重量%, 叔丁醇的含量为 2重量%, 该汽油组合物的各项技术指标参数如下表 8所 示。 对比例 9  5 parts by weight of sec-butyl acetate, 5 parts by weight of ethyl tert-butyl ether (commercially available from Guangzhou Weibo Chemical Co., Ltd., purity of 98.5 wt%), 20 parts by weight of xylene (commercially available from Sinopec Lingling Refinery, purity of 98.5 wt%) and 2 parts by weight of t-butanol (commercially available from Shanghai Xingao Chemical Reagent Co., Ltd., purity of 98.5 wt%) were added to 68 parts by weight of raw gasoline, respectively, and mixed to obtain The gasoline composition of the present invention, wherein the gasoline composition has a sec-butyl acetate content of 5% by weight, an ethyl tert-butyl ether content of 5% by weight, a xylene content of 20% by weight, and a tert-butanol content. For 2% by weight, the technical parameters of the gasoline composition are shown in Table 8 below. Comparative example 9
采用与实施例 17相同的方法制备汽油组合物, 不同的是, 不添加乙酸仲丁酯, 分 别将 10重量份的乙基叔丁基醚、 20重量份的二甲苯和 2重量份的叔丁醇分别添加到 68 重量份的原料汽油中, 混合均匀后得到汽油组合物, 该汽油组合物中乙基叔丁基醚的含 量为 10重量%, 二甲苯的含量为 20重量%, 叔丁醇的含量为 2重量%, 该汽油组合物 的各项技术指标参数如下表 8所示。 实施例 18  A gasoline composition was prepared in the same manner as in Example 17, except that sec-butyl acetate was not added, and 10 parts by weight of ethyl t-butyl ether, 20 parts by weight of xylene, and 2 parts by weight of t-butyl, respectively. The alcohol was separately added to 68 parts by weight of the raw material gasoline, and uniformly mixed to obtain a gasoline composition having a content of ethyl tert-butyl ether of 10% by weight and a content of xylene of 20% by weight, tert-butanol. The content of the gasoline composition is as shown in Table 8 below. Example 18
本实施例用来说明根据本发明的汽油组合物及其制备方法。  This embodiment is intended to illustrate a gasoline composition and a method of producing the same according to the present invention.
采用与实施例 5相同的乙酸仲丁酯和原料汽油。  The same sec-butyl acetate and raw gasoline were used as in Example 5.
将 5重量份的乙酸仲丁酯、 1重量份的甲基叔丁基醚 (商购自上海源景化学品有限 公司, 纯度为 98.5重量%)和 10重量份的二甲苯(商购自中石化长岭炼厂, 纯度为 98.5 重量%) 分别添加到 84重量份的原料汽油中, 混合均匀后得到本发明的汽油组合物, 该汽油组合物中乙酸仲丁酯的含量为 5重量%, 甲基叔丁基醚的含量为 1重量%, 二甲 苯的含量为 10重量%, 该汽油组合物的各项技术指标参数如下表 8所示。  5 parts by weight of sec-butyl acetate, 1 part by weight of methyl t-butyl ether (commercially available from Shanghai Yuanjing Chemical Co., Ltd., purity of 98.5 wt%) and 10 parts by weight of xylene (commercially available from Sinopec) Changling refinery, purity of 98.5 wt%) was added to 84 parts by weight of raw gasoline, and the mixture was uniformly mixed to obtain the gasoline composition of the present invention. The content of sec-butyl acetate in the gasoline composition was 5% by weight. The content of the tert-butyl ether was 1% by weight, and the content of xylene was 10% by weight. The technical parameters of the gasoline composition are shown in Table 8 below.
对比例 10 Comparative example 10
采用与实施例 18相同的方法制备汽油组合物, 不同的是, 不添加乙酸仲丁酯, 将 6 重量份的甲基叔丁基醚和 10重量份的二甲苯分别添加到 84重量份的原料汽油中,混合 均匀后得到汽油组合物, 该汽油组合物中甲基叔丁基醚的含量为 6重量%, 二甲苯的含 量为 10重量%, 该汽油组合物的各项技术指标参数如下表 8所示。 表 8 A gasoline composition was prepared in the same manner as in Example 18 except that sec-butyl acetate was not added, and 6 parts by weight of methyl t-butyl ether and 10 parts by weight of xylene were separately added to 84 parts by weight of the raw materials. In gasoline, after mixing, a gasoline composition is obtained. The content of methyl tert-butyl ether in the gasoline composition is 6% by weight, and the content of xylene is 10% by weight. The technical parameters of the gasoline composition are as follows: 8 is shown. Table 8
Figure imgf000023_0001
表 8 的结果表明, 乙酸仲丁酯可以与其它添加剂配合使用, 而且含有乙酸仲丁酯 的汽油组合物具有更高的辛烷值和抗爆指数。
Figure imgf000023_0001
The results in Table 8 indicate that sec-butyl acetate can be used in combination with other additives, and that the gasoline composition containing sec-butyl acetate has a higher octane number and antiknock index.

Claims

权利要求 Rights request
1、 一种汽油组合物, 其特征在于, 所述汽油组合物含有原料汽油和乙酸仲丁酯, 且以所述汽油组合物的总量计,所述乙酸仲丁酯的含量为 1-30重量%, 所述原料汽油的 含量为 70-99重量%。 A gasoline composition, characterized in that the gasoline composition contains raw gasoline and sec-butyl acetate, and the content of the sec-butyl acetate is 1-30 based on the total amount of the gasoline composition. The raw material gasoline is contained in an amount of 70 to 99% by weight.
2、 根据权利要求 1所述的汽油组合物, 其中, 以所述汽油组合物的总量计, 所述 乙酸仲丁酯的含量为 2-10重量%, 所述原料汽油的含量为 90-98重量%。 2. The gasoline composition according to claim 1, wherein the content of the sec-butyl acetate is 2 to 10% by weight based on the total amount of the gasoline composition, and the content of the raw material gasoline is 90- 98% by weight.
3、 根据权利要求 1所述的汽油组合物, 其中, 所述原料汽油含有醚系化合物、 醇 系化合物和芳烃系化合物中的一种或多种, 以所述汽油组合物的总量计, 所述汽油组合 物中的所述醚系化合物、 醇系化合物和芳烃系化合物的总量为 0.02-33重量%。 The gasoline composition according to claim 1, wherein the raw material gasoline contains one or more of an ether compound, an alcohol compound, and an aromatic compound, based on the total amount of the gasoline composition. The total amount of the ether compound, the alcohol compound, and the aromatic compound in the gasoline composition is 0.02 to 33% by weight.
4、 根据权利要求 3所述的汽油组合物, 其中, 所述芳烃系化合物为苯、 甲苯、 乙 苯、 二甲苯、 三甲苯和 C10芳烃中的一种或多种, 以所述汽油组合物的总量计, 所述芳 烃系化合物的含量为 0.02-33重量%。 The gasoline composition according to claim 3, wherein the aromatic hydrocarbon compound is one or more of benzene, toluene, ethylbenzene, xylene, trimethylbenzene and C10 aromatic hydrocarbon, and the gasoline composition The total amount of the aromatic hydrocarbon compound is 0.02 to 33% by weight.
5、 根据权利要求 3所述的汽油组合物, 其中, 所述醚系化合物为甲基叔丁基醚、 乙基叔丁基醚、 叔戊基甲醚和丁醚中的一种或多种, 以所述汽油组合物的总量计, 所述 醚系化合物的含量为 0.1-15重量%。 The gasoline composition according to claim 3, wherein the ether compound is one or more of methyl tert-butyl ether, ethyl tert-butyl ether, tert-amyl methyl ether and dibutyl ether. The ether compound is contained in an amount of from 0.1 to 15% by weight based on the total of the gasoline composition.
6、 根据权利要求 3所述的汽油组合物, 其中, 所述醇系化合物为甲醇、 乙醇、 正 丁醇、 仲丁醇和叔丁醇中的一种或多种, 以所述汽油组合物的总量计, 所述醇系化合物 的含量为 0.02-10重量%。 6. The gasoline composition according to claim 3, wherein the alcohol compound is one or more of methanol, ethanol, n-butanol, sec-butanol and tert-butanol, with the gasoline composition The total amount of the alcohol-based compound is 0.02 to 10% by weight.
7、 一种权利要求 1所述的汽油组合物的制备方法, 其特征在于, 该方法包括向原 料汽油中添加乙酸仲丁酯的步骤, 以所述汽油组合物的总量计, 所述乙酸仲丁酯的添加 量使得所述汽油组合物中的乙酸仲丁酯的含量为 1-30 重量%, 所述原料汽油的含量为 70-99重量%。 7. A method of preparing a gasoline composition according to claim 1, characterized in that the method comprises the step of adding sec-butyl acetate to the raw gasoline, the acetic acid being based on the total amount of the gasoline composition The sec-butyl ester is added in an amount such that the content of the sec-butyl acetate in the gasoline composition is from 1 to 30% by weight, and the content of the raw gasoline is from 70 to 99% by weight.
8、 根据权利要求 7所述的制备方法, 其中, 以所述汽油组合物的总量计, 所述乙 酸仲丁酯的添加量使得所述汽油组合物中的乙酸仲丁酯的含量为 2-10重量%,所述原料 汽油的含量为 90-98重量%。  8. The production method according to claim 7, wherein the sec-butyl acetate is added in an amount such that the content of sec-butyl acetate in the gasoline composition is 2 based on the total amount of the gasoline composition. The content of the raw material gasoline is -10% by weight, and the content of the raw material gasoline is from 90 to 98% by weight.
9、 根据权利要求 7或 8所述的制备方法, 其中, 所述乙酸仲丁酯的纯度不小于 80 重量%。 The production method according to claim 7 or 8, wherein the sec-butyl acetate has a purity of not less than 80% by weight.
10、 根据权利要求 7所述的制备方法, 其中, 该方法还包括向原料汽油中添加醚 系化合物、 醇系化合物和芳烃系化合物中的一种或多种的步骤, 以所述汽油组合物的总 量计, 所述汽油组合物中的所述醚系化合物、 醇系化合物和芳烃系化合物的总量为10. The preparation method according to claim 7, wherein the method further comprises adding an ether to the raw gasoline. a step of one or more of a compound, an alcohol compound, and an aromatic compound, wherein the ether compound, the alcohol compound, and the aromatic hydrocarbon compound in the gasoline composition are based on the total amount of the gasoline composition The total amount of the compound is
0.02-33重量%。 0.02-33% by weight.
11、 根据权利要求 10所述的方法, 其中, 所述醚系化合物的添加量使得所述汽油 组合物中醚系化合物的总含量为 0.1-15重量%, 所述醇系化合物的添加量使得所述汽油 组合物中醇系化合物的总含量为 0.02-10重量%, 所述芳烃系化合物的添加量使得所述 汽油组合物中芳烃系化合物的总含量为 0.02-33重量%。 The method according to claim 10, wherein the ether compound is added in an amount such that the total content of the ether compound in the gasoline composition is from 0.1 to 15% by weight, and the amount of the alcohol compound added is such that The total content of the alcohol-based compound in the gasoline composition is 0.02 to 10% by weight, and the aromatic hydrocarbon-based compound is added in an amount such that the total content of the aromatic hydrocarbon compound in the gasoline composition is 0.02 to 33% by weight.
12、 根据权利要求 10或 11所述的制备方法, 其中, 所述醚系化合物为甲基叔丁基 醚、 乙基叔丁基醚、叔戊基甲醚和丁醚中的一种或多种, 所述醇系化合物为甲醇、 乙醇、 正丁醇、 仲丁醇和叔丁醇中的一种或多种, 所述芳烃系化合物为苯、 甲苯、 乙苯、 二甲 苯、 三甲苯和 C10芳烃中的一种或多种。 The production method according to claim 10 or 11, wherein the ether compound is one or more of methyl tert-butyl ether, ethyl tert-butyl ether, tert-amyl methyl ether and dibutyl ether. The alcohol compound is one or more of methanol, ethanol, n-butanol, sec-butanol and tert-butanol, and the aromatic compounds are benzene, toluene, ethylbenzene, xylene, trimethylbenzene and C10. One or more of the aromatic hydrocarbons.
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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112646619A (en) * 2020-02-25 2021-04-13 四川华益聚能石油化工有限公司 Gasoline product oil

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104479768B (en) * 2014-12-01 2016-06-29 四川帝标新能源科技有限公司 A kind of automobile novel high-energy clean fuel oil additive and preparation method thereof
KR101869762B1 (en) * 2017-12-18 2018-06-21 한국석유관리원 complex additive agents for fuels

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2114596A (en) 1981-12-22 1983-08-24 British Petroleum Co Plc Fuel composition
CN1198466A (en) 1998-03-31 1998-11-11 苏怡鹏 Gasoline additives composition and productive method thereof
EP0905217A1 (en) 1997-09-30 1999-03-31 Nippon Oil Co. Ltd. Unleaded gasoline for direct injection gasoline engine
CN1513954A (en) 2002-11-08 2004-07-21 云 张 Formula of multifunction fuel and its production process
CN1789382A (en) * 2004-12-14 2006-06-21 上海中油企业集团有限公司 Gasoline catalytic combustion addictive
CN101240201A (en) * 2008-03-13 2008-08-13 陈家欣 Gasoline and diesel oil additive with power-increasing and energy-saving function
CN101691510A (en) * 2009-10-20 2010-04-07 济南开发区星火科学技术研究院 Novel compound gasoline antiknock agent

Family Cites Families (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2413262A (en) * 1943-05-10 1946-12-24 Union Oil Co High-compression motor fuel
US3903251A (en) * 1971-01-21 1975-09-02 Canadian Ind Gasoline production
US4440963A (en) * 1982-08-09 1984-04-03 Phillips Petroleum Company Production of MTBE and ETBE
US7462207B2 (en) * 1996-11-18 2008-12-09 Bp Oil International Limited Fuel composition
WO2001053436A1 (en) * 2000-01-24 2001-07-26 Angelica Golubkov Motor fuel for spark ignition internal combustion engines
JP4851197B2 (en) * 2006-02-17 2012-01-11 Jx日鉱日石エネルギー株式会社 Method for producing gasoline base material and gasoline composition
AU2007277154A1 (en) * 2006-07-27 2008-01-31 Mary-Louise R. Rusek Renewable engine fuel
JP5114164B2 (en) * 2006-11-07 2013-01-09 Jx日鉱日石エネルギー株式会社 Method for producing gasoline composition
JP5066434B2 (en) * 2007-12-11 2012-11-07 Jx日鉱日石エネルギー株式会社 Gasoline composition
JP5350752B2 (en) * 2008-11-12 2013-11-27 Jx日鉱日石エネルギー株式会社 Gasoline composition
JP5426237B2 (en) * 2009-05-29 2014-02-26 出光興産株式会社 Gasoline composition

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2114596A (en) 1981-12-22 1983-08-24 British Petroleum Co Plc Fuel composition
EP0905217A1 (en) 1997-09-30 1999-03-31 Nippon Oil Co. Ltd. Unleaded gasoline for direct injection gasoline engine
CN1198466A (en) 1998-03-31 1998-11-11 苏怡鹏 Gasoline additives composition and productive method thereof
CN1513954A (en) 2002-11-08 2004-07-21 云 张 Formula of multifunction fuel and its production process
CN1789382A (en) * 2004-12-14 2006-06-21 上海中油企业集团有限公司 Gasoline catalytic combustion addictive
CN101240201A (en) * 2008-03-13 2008-08-13 陈家欣 Gasoline and diesel oil additive with power-increasing and energy-saving function
CN101691510A (en) * 2009-10-20 2010-04-07 济南开发区星火科学技术研究院 Novel compound gasoline antiknock agent

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112646619A (en) * 2020-02-25 2021-04-13 四川华益聚能石油化工有限公司 Gasoline product oil

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