CN111423911A - Modified methanol gasoline vehicle fuel and preparation method thereof - Google Patents
Modified methanol gasoline vehicle fuel and preparation method thereof Download PDFInfo
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- CN111423911A CN111423911A CN202010453900.7A CN202010453900A CN111423911A CN 111423911 A CN111423911 A CN 111423911A CN 202010453900 A CN202010453900 A CN 202010453900A CN 111423911 A CN111423911 A CN 111423911A
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L1/00—Liquid carbonaceous fuels
- C10L1/02—Liquid carbonaceous fuels essentially based on components consisting of carbon, hydrogen, and oxygen only
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- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L1/00—Liquid carbonaceous fuels
- C10L1/10—Liquid carbonaceous fuels containing additives
- C10L1/14—Organic compounds
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L10/00—Use of additives to fuels or fires for particular purposes
- C10L10/04—Use of additives to fuels or fires for particular purposes for minimising corrosion or incrustation
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L10/00—Use of additives to fuels or fires for particular purposes
- C10L10/14—Use of additives to fuels or fires for particular purposes for improving low temperature properties
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L1/00—Liquid carbonaceous fuels
- C10L1/10—Liquid carbonaceous fuels containing additives
- C10L1/14—Organic compounds
- C10L1/16—Hydrocarbons
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L1/00—Liquid carbonaceous fuels
- C10L1/10—Liquid carbonaceous fuels containing additives
- C10L1/14—Organic compounds
- C10L1/16—Hydrocarbons
- C10L1/1608—Well defined compounds, e.g. hexane, benzene
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L1/00—Liquid carbonaceous fuels
- C10L1/10—Liquid carbonaceous fuels containing additives
- C10L1/14—Organic compounds
- C10L1/16—Hydrocarbons
- C10L1/1616—Hydrocarbons fractions, e.g. lubricants, solvents, naphta, bitumen, tars, terpentine
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L1/00—Liquid carbonaceous fuels
- C10L1/10—Liquid carbonaceous fuels containing additives
- C10L1/14—Organic compounds
- C10L1/18—Organic compounds containing oxygen
- C10L1/182—Organic compounds containing oxygen containing hydroxy groups; Salts thereof
- C10L1/1822—Organic compounds containing oxygen containing hydroxy groups; Salts thereof hydroxy group directly attached to (cyclo)aliphatic carbon atoms
- C10L1/1824—Organic compounds containing oxygen containing hydroxy groups; Salts thereof hydroxy group directly attached to (cyclo)aliphatic carbon atoms mono-hydroxy
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L1/00—Liquid carbonaceous fuels
- C10L1/10—Liquid carbonaceous fuels containing additives
- C10L1/14—Organic compounds
- C10L1/18—Organic compounds containing oxygen
- C10L1/182—Organic compounds containing oxygen containing hydroxy groups; Salts thereof
- C10L1/183—Organic compounds containing oxygen containing hydroxy groups; Salts thereof at least one hydroxy group bound to an aromatic carbon atom
- C10L1/1832—Organic compounds containing oxygen containing hydroxy groups; Salts thereof at least one hydroxy group bound to an aromatic carbon atom mono-hydroxy
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L1/00—Liquid carbonaceous fuels
- C10L1/10—Liquid carbonaceous fuels containing additives
- C10L1/14—Organic compounds
- C10L1/22—Organic compounds containing nitrogen
- C10L1/222—Organic compounds containing nitrogen containing at least one carbon-to-nitrogen single bond
- C10L1/223—Organic compounds containing nitrogen containing at least one carbon-to-nitrogen single bond having at least one amino group bound to an aromatic carbon atom
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L2230/00—Function and purpose of a components of a fuel or the composition as a whole
- C10L2230/22—Function and purpose of a components of a fuel or the composition as a whole for improving fuel economy or fuel efficiency
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L2270/00—Specifically adapted fuels
- C10L2270/02—Specifically adapted fuels for internal combustion engines
- C10L2270/023—Specifically adapted fuels for internal combustion engines for gasoline engines
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- Liquid Carbonaceous Fuels (AREA)
Abstract
The invention discloses a modified methanol gasoline vehicle fuel and a preparation method thereof, wherein the raw materials of the modified methanol gasoline vehicle fuel comprise 50-70% of methanol, 0.5-1% of solvent naphtha, 10-15% of cosolvent and the balance of gasoline, wherein the cosolvent is composed of aniline or derivatives thereof, C6-C10 alkane, styrene, phenol, n-amyl alcohol and n-octyl alcohol. The form of the modified methanol gasoline vehicle fuel is a uniform oil phase, the combustion performance of the modified methanol gasoline vehicle fuel is far higher than that of microemulsion methanol gasoline, the safety performance is relatively higher, the cost is low, a surfactant is not required to be used, and the modified methanol gasoline vehicle fuel can be used by a common gasoline engine without modification.
Description
Technical Field
The invention relates to the technical field of methanol gasoline processing, in particular to a modified methanol gasoline vehicle fuel and a preparation method thereof.
Background
Methanol is a colorless, transparent, flammable and volatile liquid, can be made from coal and coke, and a small amount of methanol is recovered as a byproduct from the dry distillation of wood.
At present, methanol gasoline is prepared by adding part of methanol into gasoline and compounding the methanol gasoline with a methanol fuel cosolvent, and has the characteristics of good thermal efficiency, dynamic property and economy, emission reduction, petroleum saving, safety, convenience and the like. However, methanol has great differences from gasoline in physical and chemical properties, and the differences cause that the content of methanol in the methanol gasoline is relatively low, and the application of the methanol gasoline on automobiles has the following problems:
(1) the number of carbon atoms and hydrogen atoms in methanol molecules is different from that of gasoline, and the methanol molecules contain oxygen atoms, so that compared with the gasoline, the fuel cannot be ignited due to the fact that the concentration of the mixed gas is too lean under the condition of the same engine air inflow;
(2) the latent heat of vaporization of the methanol is 3.6 times that of the gasoline, and the high latent heat of vaporization and the lower vapor pressure cause the difficulty of cold start of the engine;
(3) methanol has swelling effect on non-metal materials such as plastics and rubber, and has corrosiveness on metal materials such as lead, tin, aluminum, copper and iron.
Therefore, the methanol gasoline used on the common gasoline engine needs to increase the fuel injection amount, increase the injection pulse width and replace the equipment or adjust the parameters of the traditional gasoline engine so as to use the methanol gasoline as the replacement fuel.
In patent CN101914396B, a methanol gasoline fuel is disclosed, which is prepared by modifying methanol to combine with a cosolvent and gasoline to obtain a novel fuel without modifying a gasoline engine, and the fuel has good combustion performance, and the addition of modified methanol is improved to a certain extent compared with the existing level. However, the methanol gasoline is in a micro-emulsion form, a large amount of surfactant is required to be used, and the combustion performance of the fuel in the micro-emulsion form is far lower than that of the fuel in a uniform oil phase. The research of the researchers of the invention is to improve the process and the formula to obtain the oil-phase methanol gasoline without modifying the gasoline engine.
Disclosure of Invention
Based on the problems, the invention aims to provide a modified methanol gasoline vehicle fuel, which is in a form of a uniform oil phase, has far higher combustion performance than microemulsion methanol gasoline, relatively higher safety performance and low cost, and does not need to use a surfactant.
The modified methanol gasoline vehicle fuel comprises the following raw materials in percentage by weight:
50-70 percent of methanol
Solvent oil 0.5-1%
10 to 15 percent of cosolvent
The rest is gasoline,
the cosolvent is composed of aniline or its derivatives, C6-C10 alkane, styrene, phenol, n-pentanol, and n-octanol.
Specifically, the gasoline of the invention is 90#-97#Commercial gasoline.
Specifically, the aniline derivative of the present invention is one of p-toluidine and o-toluidine.
Specifically, the C6-C10 alkane is at least one of 2, 3-methylbutane, 2-methyl-3-ethylpentane, 2-methyl-3-isopropyl-pentane, n-hexane, n-heptane and 2, 4-methylpentane.
Specifically, the weight ratio of the aniline or the derivative thereof, C6-C10 alkane, styrene, phenol, n-amyl alcohol and n-octyl alcohol is 1:1-3:5-7:1-3:3-9: 2-5.
The preparation method of the modified methanol gasoline vehicle fuel comprises the following steps:
(1) weighing aniline or its derivatives, C6-C10 alkane, styrene, phenol, n-pentanol, and n-octanol according to a certain proportion, mixing, and stirring for 10-20min to obtain cosolvent;
(2) weighing solvent oil, and pouring the solvent oil into a cosolvent while stirring;
(3) slowly pouring the mixed solution in the step (2) into methanol at low temperature, and stirring for 5-10min at low temperature;
(4) and (4) finally, slowly pouring the mixed raw materials obtained in the step (3) into gasoline while stirring to obtain the modified methanol gasoline.
Specifically, the low temperature in step (3) of the present invention is 5 to 10 ℃.
Compared with the prior art, the invention has the following beneficial effects:
according to the invention, through adjusting the raw material composition of the methanol gasoline, the raw materials have very good mutual dissolving effect, the stability of the raw materials is improved, and the methanol and the gasoline can be fully dissolved;
the modified methanol gasoline has good corrosion resistance, can form a good protective film with the surface of metal, and effectively avoids the corrosion of the metal;
the modified methanol gasoline vehicle fuel has strong adaptability to the environmental temperature, and can be used in the environment with the temperature of-40 ℃ to 40 ℃;
the modified methanol gasoline vehicle fuel has high combustion rate and thermal efficiency, and greatly reduces oil consumption.
Detailed Description
The present invention will be further described with reference to the following specific examples.
Example 1
The preparation process of the modified methanol gasoline vehicle fuel comprises the following steps:
firstly, weighing aniline, 2, 4-methylpentane, styrene, phenol, n-amyl alcohol and n-octyl alcohol in a weight ratio of 1:1:5:2:3:4, mixing and fully stirring for 20min to obtain a cosolvent;
secondly, weighing 10g of cosolvent and 1g of solvent oil, and pouring the solvent oil into the cosolvent while stirring to obtain a mixed solution I;
thirdly, slowly pouring the mixed solution I into 70g of methanol at the temperature of 5 ℃, and stirring for 10min at the temperature to obtain a mixed solution II;
finally, the mixture II was slowly poured into 19g 92 at room temperature under stirring#Obtaining the modified methanol gasoline vehicle fuel from commercial gasoline.
Example 2
The preparation process of the modified methanol gasoline vehicle fuel comprises the following steps:
firstly, weighing o-toluidine, 2-methyl-3-isopropyl-pentane, styrene, phenol, n-amyl alcohol and n-octyl alcohol in a weight ratio of 1:3:7:1:9:5, mixing and fully stirring for 20min to obtain a cosolvent;
secondly, weighing 10g of cosolvent and 1g of solvent oil, and pouring the solvent oil into the cosolvent while stirring to obtain a mixed solution I;
thirdly, slowly pouring the mixed solution I into 69g of methanol at the temperature of 10 ℃, and stirring for 10min at the temperature to obtain a mixed solution II;
finally, the mixture II was slowly poured into 20g of 92 g of the mixture II at room temperature while stirring#Obtaining the modified methanol gasoline vehicle fuel from commercial gasoline.
Example 3
The preparation process of the modified methanol gasoline vehicle fuel comprises the following steps:
firstly, weighing p-toluidine, 2-methyl-3-ethylpentane, styrene, phenol, n-amyl alcohol and n-octyl alcohol in a weight ratio of 1:2:5:1:7:3, mixing and fully stirring for 20min to obtain a cosolvent;
secondly, weighing 15g of cosolvent and 1g of solvent oil, and pouring the solvent oil into the cosolvent while stirring to obtain a mixed solution I;
thirdly, slowly pouring the mixed solution I into 54g of methanol at the temperature of 5 ℃, and stirring for 5min at the temperature to obtain a mixed solution II;
finally, the mixture II was slowly poured into 30g of 92 at room temperature while stirring#Obtaining the modified methanol gasoline vehicle fuel from commercial gasoline.
Example 4
The preparation process of the modified methanol gasoline vehicle fuel comprises the following steps:
firstly, weighing p-toluidine, n-heptane, styrene, phenol, n-pentanol and n-octanol according to the weight ratio of 1:3:5:2:8:2, mixing and fully stirring for 10min to obtain a cosolvent;
secondly, weighing 10g of cosolvent and 0.5g of solvent oil, and pouring the solvent oil into the cosolvent while stirring to obtain a mixed solution I;
thirdly, slowly pouring the mixed solution I into 50g of methanol at the temperature of 5 ℃, and stirring for 5min at the temperature to obtain a mixed solution II;
finally, the mixture II was slowly poured into a flask at room temperature to 39.5g 92 with stirring#Obtaining the modified methanol gasoline vehicle fuel from commercial gasoline.
Example 5
The preparation process of the modified methanol gasoline vehicle fuel comprises the following steps:
firstly, weighing aniline, n-hexane, styrene, phenol, n-pentanol and n-octanol according to the weight ratio of 1:2:6:1:4:3, mixing and fully stirring for 10min to obtain a cosolvent;
secondly, weighing 12g of cosolvent and 0.5g of solvent oil, and pouring the solvent oil into the cosolvent while stirring to obtain a mixed solution I;
thirdly, slowly pouring the mixed solution I into 70g of methanol at the temperature of 10 ℃, and stirring for 10min at the temperature to obtain a mixed solution II;
finally, the mixture II was slowly poured into a flask of 17.5g 92 at room temperature while stirring#Obtaining modified methanol gasoline vehicle from commercial gasolineAnd (3) fuel.
Comparative example 1
According to the preparation process of the example 2, a cosolvent is prepared by adopting o-toluidine, styrene, phenol, n-amyl alcohol and n-octyl alcohol, the weight ratio of the five raw materials is 1:7:1:9:5, and the other processes are the same as the example 2, so that the methanol gasoline fuel is prepared.
Comparative example 2
According to the preparation process of the example 2, a methanol gasoline fuel is prepared by adopting 2-methyl-3-isopropyl-pentane, styrene, phenol, n-amyl alcohol and n-octanol to prepare a cosolvent, wherein the weight ratio of the five raw materials is 3:7:1:9:5, and the other processes are the same as the example 2.
Comparative example 3
According to the preparation process of the embodiment 2, a methanol gasoline fuel is prepared by adopting o-toluidine, 2-methyl-3-isopropyl-pentane, styrene and phenol as a cosolvent, wherein the weight ratio of the four raw materials is 1:3:7:1, and the rest processes are the same as the embodiment 2.
Comparative example 4
The preparation process of the embodiment 3 of the patent CN101914396B is used for obtaining the methanol gasoline microemulsion for the vehicle, and the preparation process comprises the following steps:
(1) preparing modified methanol:
adding 5Kg of methanol into a reaction kettle, adding 120g of span 85, 35g of span 65, 20g of tween 85, 150g of methyl tert-butyl ether, 50g of isopropyl ether, 250g of imidazoline amide, 1g of 2, 6-di-tert-butyl-p-cresol and 1g of industrial anticorrosive 1201 under the stirring condition, and stirring until the solution is clear and transparent after the addition is finished to obtain modified methanol;
(2) and (3) preparation of a cosolvent:
adding 5Kg of butanol, 1Kg of m-xylene, 1Kg of n-octanol and 1Kg of isopropanol into a reaction kettle, and stirring until the mixture is uniformly mixed to obtain a cosolvent;
(3) preparing the methanol gasoline microemulsion for the vehicle:
to the modified methanol thus prepared, 5Kg 92 was added#Adding 2.5Kg of the prepared cosolvent into commercial gasoline under the condition of violent stirring, and continuously stirring until the solution is clear and transparent to obtain the methanol gasoline for vehiclesAnd (3) micro-emulsion.
The methanol gasoline motor fuels prepared in examples 1 to 5 and comparative examples 1 to 4 of the present application were tested, and the test results are shown in table 1.
TABLE 1
Heat value | Whether the gasoline engine needs to be modified | |
Example 1 | 3.61×104KJ/Kg | Whether or not |
Example 2 | 4.02×104KJ/Kg | Whether or not |
Example 3 | 3.73×104KJ/Kg | Whether or not |
Example 4 | 3.90×104KJ/Kg | Whether or not |
Example 5 | 3.85×104KJ/Kg | Whether or not |
Comparative example 1 | 2.99×104KJ/Kg | Is that |
Comparative example 2 | 3.17×104KJ/Kg | Is that |
Comparative example 3 | 3.04×104KJ/Kg | Is that |
Comparative example 4 | 2.84×104KJ/Kg | Whether or not |
The anti-knock property and the anti-corrosion property of the methanol gasoline car fuel obtained in the examples 1 to 5 of the present invention are also higher than those of the comparative examples 1 to 4.
The principles and embodiments of the present invention have been described herein using specific examples, which are provided only to help understand the method and the core concept of the present invention; meanwhile, for a person skilled in the art, according to the idea of the present invention, the specific embodiments and the application range may be changed. In view of the above, the present disclosure should not be construed as limiting the invention.
Claims (7)
1. The modified methanol gasoline vehicle fuel is characterized by comprising the following raw materials in percentage by weight:
50-70 percent of methanol
Solvent oil 0.5-1%
10 to 15 percent of cosolvent
The rest is gasoline,
the cosolvent is composed of aniline or its derivatives, C6-C10 alkane, styrene, phenol, n-pentanol, and n-octanol.
2. The modified methanol gasoline vehicle fuel of claim 1, wherein the gasoline is 90 gasoline#-97#Commercial gasoline.
3. The modified methanol gasoline vehicle fuel of claim 1, wherein the aniline derivative is one of p-toluidine and o-toluidine.
4. The modified methanol gasoline vehicle fuel of claim 1, wherein the C6-C10 alkane is at least one of 2, 3-methylbutane, 2-methyl-3-ethylpentane, 2-methyl-3-isopropyl-pentane, n-hexane, n-heptane, and 2, 4-methylpentane.
5. The modified methanol gasoline car fuel of claim 1, wherein the weight ratio of aniline or its derivative, C6-C10 alkane, styrene, phenol, n-pentanol, n-octanol is 1:1-3:5-7:1-3:3-9: 2-5.
6. The method of any one of claims 1 to 5, comprising the steps of:
(1) weighing aniline or its derivatives, C6-C10 alkane, styrene, phenol, n-pentanol, and n-octanol according to a certain proportion, mixing, and stirring for 10-20min to obtain cosolvent;
(2) weighing solvent oil according to a proportion, and pouring the solvent oil into a cosolvent while stirring;
(3) slowly pouring the mixed solution in the step (2) into methanol at low temperature, and stirring for 5-10min at low temperature;
(4) and (4) finally, slowly pouring the mixed raw materials obtained in the step (3) into gasoline while stirring to obtain the modified methanol gasoline.
7. The method for preparing the modified methanol gasoline vehicle fuel as claimed in claim 6, wherein the low temperature in the step (3) is 5-10 ℃.
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
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CN112500894A (en) * | 2020-10-27 | 2021-03-16 | 湖南红宝科技开发有限公司 | Modified methanol gasoline and preparation method thereof |
CN112812865A (en) * | 2021-01-11 | 2021-05-18 | 南通腾展新能源科技有限公司 | Fuel oil power agent |
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2020
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Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
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CN112500894A (en) * | 2020-10-27 | 2021-03-16 | 湖南红宝科技开发有限公司 | Modified methanol gasoline and preparation method thereof |
CN112812865A (en) * | 2021-01-11 | 2021-05-18 | 南通腾展新能源科技有限公司 | Fuel oil power agent |
CN112812865B (en) * | 2021-01-11 | 2023-07-14 | 南通鑫纳尔油品有限公司 | Fuel oil power agent |
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Application publication date: 20200717 |