CN101270305B - Methanol gasoline - Google Patents
Methanol gasoline Download PDFInfo
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- CN101270305B CN101270305B CN2008100162369A CN200810016236A CN101270305B CN 101270305 B CN101270305 B CN 101270305B CN 2008100162369 A CN2008100162369 A CN 2008100162369A CN 200810016236 A CN200810016236 A CN 200810016236A CN 101270305 B CN101270305 B CN 101270305B
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- methyl alcohol
- butanols
- tert
- acetone
- methanol gasoline
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Abstract
The invention discloses methanol gasoline, which eases the shortage of energy sources. The methanol gasoline is prepared with methanol, oil and an additive. The quality index of the product is the same with the quality index of pure gasoline, and the product contains oxygen without sulfur. The methanol gasoline has the characteristics of no corrosion, good combustion performance, releasing heat quickly, high thermal efficiency, good combustion and working power for a petrol motor and so on. In addition, as methanol is used as the main raw material, the methanol gasoline is low in cost and has beneficial result.
Description
Technical field
The present invention relates to the technical field of vehicle fuel, be specifically related to a kind of automobile fuel methanol gasoline of cleaning.
Background technology
Along with the rapid economy development in the world, powerful further to demands for energy, particularly domestic economy is in the status in the world and fast-developing needs, and is just more urgent to demands for energy.The Energy Situation of China is that the energy fuel of petroleum-type is deficient, so the substitute energy of the fuel of development petroleum-type is the needs and the requirement of present national energy development strategy.Present on the market methanol gasoline, owing to receive the restriction of the physicochemical property of methyl alcohol, more or less some problems all reduces, meets many technical barriers such as water stratification, cold start-up difficulty like corrodibility, swelling property, vapour lock, power to material.
Summary of the invention
The methanol gasoline that the objective of the invention is to process can be alleviated the short situation that the energy is badly in need of to a certain extent.Concrete implementation method of the present invention is that the component of this methanol gasoline by volume per-cent is component oil 15～85%, additive 3%～10%, methyl alcohol surplus.The methyl alcohol component is an industrial methanol, purity >=97%.
Additive is in harmonious proportion formulated by following raw materials according, various raw materials shared volume percent in methanol gasoline is following:
Organic luxuriant 0.3%～0.9%, acetone 0.3%～1.3%, butanols 0.6%～1.7%, YLENE 0.6%～2.1%, ethylbenzene 0.6%～2%, metal corrosion inhibitor 0.1%～0.5%, 2,6-di-tert-butyl methyl phenol 0.5%～1.5%.
Component oil is: any in 90# gasoline, petroleum naphtha, solvent oil, pentane, heptane and the octane.
Advantage of the present invention: organic luxuriant in the above-mentioned prescription can replenish that part of by the methyl alcohol dilution of gasoline octane rating, increases the stability and the dynamic property of methanol gasoline; The acetone mutual solubility is good; The butanols calorific value is high, and solvability is good, has good oxidation-resistance; 2, the 6-di-tert-butyl methyl phenol has good oxidation-resistance, wear resisting property.So adopt that this methanol gasoline has that octane value height, consistency are good, sufficient combustion, anti-seismic performance is good, dynamic property is strong.Because main raw material is a methyl alcohol, 90# gasoline (or any in petroleum naphtha, solvent oil, pentane, heptane and the octane) is so this kind methanol gasoline cost is lower.In the such scheme: metal corrosion inhibitor is the commercially available prod.
Embodiment
Embodiment 1:
Following raw material joined in the one-level mixing tank according to volume percent stir: 90# gasoline 15%, organic luxuriant 0.9%, acetone 1.3%, butanols 1.7%, YLENE 2.1%, ethylbenzene 2%, metal corrosion inhibitor 0.5%, 2; 6-di-tert-butyl methyl phenol 1.5%, methyl alcohol surplus; It is subsequent use to inject the secondary jar with pump again; Promptly accomplish configuration effort, obtain finished product after leaving standstill.
Embodiment 2:
Following raw material joined in the one-level mixing tank according to volume percent stir: petroleum naphtha 85%, organic luxuriant 0.3%, acetone 0.3%, butanols 0.6%, YLENE 0.6%, ethylbenzene 0.6%, metal corrosion inhibitor 0.1%, 2; 6-di-tert-butyl methyl phenol 0.5%, methyl alcohol surplus; It is subsequent use to inject the secondary jar with pump again; Promptly accomplish configuration effort, obtain finished product after leaving standstill.
Embodiment 3:
Following raw material joined in the one-level mixing tank according to volume percent stir: solvent oil 85%, organic luxuriant 0.3%, acetone 0.3%, butanols 0.6%, YLENE 0.6%, ethylbenzene 0.6%, metal corrosion inhibitor 0.1%, 2; 6-di-tert-butyl methyl phenol 0.5%, methyl alcohol surplus; It is subsequent use to inject the secondary jar with pump again; Promptly accomplish configuration effort, obtain finished product after leaving standstill.
Embodiment 4:
Following raw material joined in the one-level mixing tank according to volume percent stir: pentane 85%, organic luxuriant 0.3%, acetone 0.3%, butanols 0.6%, YLENE 0.6%, ethylbenzene 0.6%, metal corrosion inhibitor 0.1%, 2; 6-di-tert-butyl methyl phenol 0.5%, methyl alcohol surplus; It is subsequent use to inject the secondary jar with pump again; Promptly accomplish configuration effort, obtain finished product after leaving standstill.
Embodiment 5:
Following raw material joined in the one-level mixing tank according to volume percent stir: octane 70%, organic luxuriant 0.5%, acetone 0.8%, butanols 1%, YLENE 1%, ethylbenzene 1%, metal corrosion inhibitor 0.2%, 2; 6-di-tert-butyl methyl phenol 1%, methyl alcohol surplus; It is subsequent use to inject the secondary jar with pump again; Promptly accomplish configuration effort, obtain finished product after leaving standstill.
Embodiment 6:
Following raw material joined in the one-level mixing tank according to volume percent stir: heptane 50%, organic luxuriant 0.7%, acetone 1%, butanols 1.5%, YLENE 1.5%, ethylbenzene 1.5%, metal corrosion inhibitor 0.5%, 2; 6-di-tert-butyl methyl phenol 1.5%, methyl alcohol surplus; It is subsequent use to inject the secondary jar with pump again; Promptly accomplish configuration effort, obtain finished product after leaving standstill.
Claims (7)
1. methanol gasoline, it is characterized in that: its component comprises methyl alcohol, component oil and additive; Each component by volume per-cent is: component oil 15%～85%, organic luxuriant 0.3%～0.9%, acetone 0.3%～1.3%, butanols 0.6%～1.7%, YLENE 0.6%～2.1%, ethylbenzene 0.6%～2%, metal corrosion inhibitor 0.1%～0.5%, 2,6-di-tert-butyl methyl phenol 0.5%～1.5%, methyl alcohol surplus; The methyl alcohol component is an industrial methanol, purity >=97%; Said component oil is: any in 90# gasoline, petroleum naphtha, solvent oil, pentane, heptane and the octane.
2. methanol gasoline according to claim 1; It is characterized in that: following raw material is joined in the one-level mixing tank according to volume percent stir: 90# gasoline 15%, organic luxuriant 0.9%, acetone 1.3%, butanols 1.7%, YLENE 2.1%, ethylbenzene 2%, metal corrosion inhibitor 0.5%, 2; 6-di-tert-butyl methyl phenol 1.5%, methyl alcohol surplus; It is subsequent use to inject the secondary jar with pump again, promptly accomplishes configuration effort, obtains finished product after leaving standstill.
3. methanol gasoline according to claim 1; It is characterized in that: following raw material is joined in the one-level mixing tank according to volume percent stir: petroleum naphtha 85%, organic luxuriant 0.3%, acetone 0.3%, butanols 0.6%, YLENE 0.6%, ethylbenzene 0.6%, metal corrosion inhibitor 0.1%, 2; 6-di-tert-butyl methyl phenol 0.5%, methyl alcohol surplus; It is subsequent use to inject the secondary jar with pump again, promptly accomplishes configuration effort, obtains finished product after leaving standstill.
4. methanol gasoline according to claim 1; It is characterized in that: following raw material is joined in the one-level mixing tank according to volume percent stir: solvent oil 85%, organic luxuriant 0.3%, acetone 0.3%, butanols 0.6%, YLENE 0.6%, ethylbenzene 0.6%, metal corrosion inhibitor 0.1%, 2; 6-di-tert-butyl methyl phenol 0.5%, methyl alcohol surplus; It is subsequent use to inject the secondary jar with pump again, promptly accomplishes configuration effort, obtains finished product after leaving standstill.
5. methanol gasoline according to claim 1; It is characterized in that: following raw material is joined in the one-level mixing tank according to volume percent stir: pentane 85%, organic luxuriant 0.3%, acetone 0.3%, butanols 0.6%, YLENE 0.6%, ethylbenzene 0.6%, metal corrosion inhibitor 0.1%, 2; 6-di-tert-butyl methyl phenol 0.5%, methyl alcohol surplus; It is subsequent use to inject the secondary jar with pump again, promptly accomplishes configuration effort, obtains finished product after leaving standstill.
6. methanol gasoline according to claim 1; It is characterized in that: following raw material is joined in the one-level mixing tank according to volume percent stir: octane 70%, organic luxuriant 0.5%, acetone 0.8%, butanols 1%, YLENE 1%, ethylbenzene 1%, metal corrosion inhibitor 0.2%, 2; 6-di-tert-butyl methyl phenol 1%, methyl alcohol surplus; It is subsequent use to inject the secondary jar with pump again, promptly accomplishes configuration effort, obtains finished product after leaving standstill.
7. methanol gasoline according to claim 1; It is characterized in that: following raw material is joined in the one-level mixing tank according to volume percent stir: heptane 50%, organic luxuriant 0.7%, acetone 1%, butanols 1.5%, YLENE 1.5%, ethylbenzene 1.5%, metal corrosion inhibitor 0.5%, 2; 6-di-tert-butyl methyl phenol 1.5%, methyl alcohol surplus; It is subsequent use to inject the secondary jar with pump again, promptly accomplishes configuration effort, obtains finished product after leaving standstill.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2008100162369A CN101270305B (en) | 2008-05-19 | 2008-05-19 | Methanol gasoline |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2008100162369A CN101270305B (en) | 2008-05-19 | 2008-05-19 | Methanol gasoline |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN101270305A CN101270305A (en) | 2008-09-24 |
| CN101270305B true CN101270305B (en) | 2012-01-11 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2008100162369A Active CN101270305B (en) | 2008-05-19 | 2008-05-19 | Methanol gasoline |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN101270305B (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101928610B (en) * | 2010-09-01 | 2013-03-13 | 桂林腾翔新能源科技有限公司 | Synthetic fuel for vehicles |
| CN102199456A (en) * | 2011-04-19 | 2011-09-28 | 姜立广 | Biological liquid fuel |
| CN110823949B (en) * | 2019-09-25 | 2020-08-28 | 西安交通大学 | Method for rapidly calculating octane value sensitivity of ethanol gasoline based on heat release rate curve |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1621500A (en) * | 2004-11-03 | 2005-06-01 | 肖丽 | Environment protection type methanol gasoline |
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2008
- 2008-05-19 CN CN2008100162369A patent/CN101270305B/en active Active
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1621500A (en) * | 2004-11-03 | 2005-06-01 | 肖丽 | Environment protection type methanol gasoline |
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| CN101270305A (en) | 2008-09-24 |
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