CN101195771A - Composite gasoline of methanol and method for producing the same - Google Patents
Composite gasoline of methanol and method for producing the same Download PDFInfo
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- CN101195771A CN101195771A CNA2007101798254A CN200710179825A CN101195771A CN 101195771 A CN101195771 A CN 101195771A CN A2007101798254 A CNA2007101798254 A CN A2007101798254A CN 200710179825 A CN200710179825 A CN 200710179825A CN 101195771 A CN101195771 A CN 101195771A
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Abstract
The invention discloses methanol compound gasoline, the methanol compound gasoline is composed of methanol, gasoline, propanone, ethylether, tertiary butyl alcohol, nitric acid cerous cerium, isopropyl alcohol and combined additive agent. The preparation method of the invention is to perform the convection to the methanol, the gasoline, the propanone, the ethylether, the tertiary butyl alcohol, the nitric acid cerous cerium, the isopropyl alcohol and the combined additive agent from different directions and to inject into a mixing tank simultaneously, an oil pump is used to inject the all to the mixing tank, the circulating oil pump is used in the tank to perform the mixing and circulating, finally, the preparation is finished after the oil pump is used to inject into a finished product oil tank. The methanol compound gasoline of the invention can solve a series of problems that the mechanical performance, the dynamic performance, the safety performance and the starting performance of vehicles are bad. Simultaneously, the invention can simultaneously perform the function of the cleanness and the environment protection, and the advantages of reducing the gasoline cost and reducing the fuel oil consumption of the vehicles.
Description
Technical field
The present invention relates to a kind of methanol composite gasoline, particularly a kind of automobile methanol composite gasoline of high-cleanness environment-friendly and preparation method thereof.
Background technology
Along with the Domestic Automotive Industry fast development, it is severe that these two important problem of environmental pollution and energy scarcity will more show.Nearly 7,000 hundred million tons of China's coal reserves, 2,200,000,000 tons of annual consumption can be used 200-300 for China, press present situation China's oil consumption in 2004 at 3.17 hundred million tons, and the domestic production amount only have 1.76 hundred million tons, and the net importation amount is 1.51 hundred million tons, and externally interdependency is 47.3%.Thereby the serious situation of the shortage of China's oil as can be seen.
Automobile has also brought environmental issue when promoting economic boom, bringing convenience to people's lives.Wherein to the environmental influence maximum, no more than serious day by day automobile exhaust pollution along with the growth at full speed of motor vehicle total amount.In Beijing, big cities such as Shanghai, Guangzhou, motor vehicle has become the first source of pollution of pollutents such as discharging carbon monoxide, oxynitride, hydrocarbon polymer.The insider estimates that the automobile pollution of China may be above 100,000,000 after 10 years-15 years.Therefore, administering auto-pollution will be secular, arduous, a complicated system engineering.
The effective way that addresses these problems is: take the fuel economy consumption significantly of policy and technical measures; The various cleaning alternative fuel of Application and Development.
Hydrogen Energy is as the energy carrier the same with electricity, and alternative in theory fossil fuel solve energy problem, but in fact Hydrogen Energy economy is far away.From the hydrogen production to the transportation, to using hydrogen to make the automobile of the energy, these investments are added up needs last trillion dollars input, is not the most real a kind of implementation from the hydrogen gas station.
China is the whole world the 3rd mcroorganism fuel ethanol production and country of consumption after Brazil, the U.S. at present.It is reported, progressively popularization along with alcohol fuel, China is that the alcohol fuel output of raw material soars all the way to 1,320,000 tons of 2006 from 70,000 tons in 2003 with the grain in storage for years, if produce 1 ton of alcohol fuel conversion by per 3.3 tons of corns, only just consumes 4,360,000 tons of corns in 2006.Yet, the corn of the ethanol that acts as a fuel in the recent period main raw material is in that supply falls short of demand state, die-offing of corn stock soared domestic corn price, and the hidden danger of striving food with the people appears in alcohol fuel, ensures that national food safety becomes the severe problem of pendulum in face of government.The expert analyzes, and China is populous, and the per capita cultivated land is few, with a large amount of grain-production alcohol fuels must and the people " strives food ", he " strives the soil ", cause the human living space more and more littler, do not meet China's national situation.
For the raw material production alcohol fuel does not meet national conditions, exploring non-grain Energy resources is trends of the times with grain.Brazil that present alcohol fuel development scale is in the prostatitis uses the sugarcane production alcohol fuel, and the U.S. uses the Maize Production alcohol fuel.But China does not possess the condition of extensive use sugarcane or corn, and along with starting of policy restriction corn processed project, industry must be sought the fuel source beyond the corn.
Summary of the invention
The objective of the invention is to disclose a kind of methanol composite gasoline;
The present invention also aims to disclose the preparation method of this methanol composite gasoline.
The present invention is achieved through the following technical solutions:
The component of methanol composite gasoline of the present invention is:
Methyl alcohol 10-60 weight part gasoline 10-65 weight part
Acetone 1-5 weight part ether 1-8 weight part
Trimethyl carbinol 1-4 weight part cerous nitrate 1-5 weight part
Virahol 1-5 weight part combined additive 1-10 weight part;
Wherein the component of combined additive is: active zinc flower 0.4-4 weight part, isopropyl nitrate 0.3-2.4 weight part, triamine 0.18-3 weight part, dimethylbenzene 0.02-0.1 weight part, hydrogen peroxidase 10 .1-0.5 weight part.
The component of methanol composite gasoline of the present invention is preferably:
Methyl alcohol 35 weight part gasoline 40 weight part acetone 4 weight parts
The ether 7 weight part trimethyl carbinols 4 weight part cerous nitrates 2 weight parts
Virahol 2 weight part combined additives 6 weight parts;
Wherein the component of combined additive is: active zinc flower 2.6 weight parts, isopropyl nitrate 1.5 weight parts, triamine 1.5 weight parts, dimethylbenzene 0.08 weight part, hydrogen peroxidase 10 .32 weight part.
The component of methanol composite gasoline of the present invention is preferably:
Methyl alcohol 35 weight part gasoline 38 weight parts
Acetone 3 weight part ether 4.5 weight parts
The trimethyl carbinol 2.5 weight part cerous nitrates 3 weight parts
Virahol 3 weight part combined additives 5.5 weight parts;
Wherein the component of combined additive is: active zinc flower 2.2 weight parts, isopropyl nitrate 1.35 weight parts, triamine 1.59 weight parts, dimethylbenzene 0.06 weight part, hydrogen peroxidase 10 .3 weight part.
The component of methanol composite gasoline of the present invention is preferably:
Acetone 4.5 weight part ether 1.5 weight parts
The trimethyl carbinol 1.5 weight part cerous nitrates 4.5 weight parts
Virahol 4.5 weight part combined additives 1.5 weight parts.
Wherein the component of combined additive is: active zinc flower 0.5 weight part, isopropyl nitrate 0.5 weight part, triamine 0.2 weight part, dimethylbenzene 0.03 weight part, hydrogen peroxidase 10 .27 weight part.
The component of methanol composite gasoline of the present invention is preferably:
Methyl alcohol 45 weight part gasoline 25 weight parts
Acetone 2 weight part ether 5 weight parts
The trimethyl carbinol 1.5 weight part cerous nitrates 2 weight parts
Virahol 2 weight part combined additives 7 weight parts.
Wherein the component of combined additive is: active zinc flower 3 weight parts, isopropyl nitrate 2 weight parts, triamine 1.5 weight parts, dimethylbenzene 0.08 weight part, hydrogen peroxidase 10 .42 weight part.
Described gasoline is the homemade petrochemical industry gasoline of 90#, the homemade petrochemical industry gasoline of 93# or the homemade petrochemical industry gasoline of 97#.
The preparation method of methanol composite gasoline of the present invention is:
Methyl alcohol, gasoline, acetone, ether, the trimethyl carbinol, cerous nitrate, Virahol and combined additive are injected mixing tank simultaneously by the convection current from different directions of Different Weight part, when each ingredients substance all in proportion the filling finish after, all inject mixing tank again with oil pump, in jar, use circulating oil pump to carry out mixed cycle 20-30 minute, promptly prepare with oil pump injection product tank at last and finish.
Another preparation method of methanol composite gasoline of the present invention comprises the steps:
1) methyl alcohol is imported additive tank 1, cover sealing cover 17, additive pump input control valve 19 on the opening conduits 9i and additive pump output control 20, simultaneously the output control valve 11 on the pipeline 9 is opened, and the input control valve 10 of the pipeline 9a on the methanol tank 2 opened, methyl alcohol is from the additive tank 1 pipeline 9i that flows through, and to export methyl alcohol to methanol tank 2 through pipeline 9 and 9a standby for the pressure by additive pump 18 again;
2) with acetone, ether, the trimethyl carbinol, cerous nitrate, Virahol input additive tank 1, cover sealing cover 17, additive pump input control valve 19 on the opening conduits 9i and additive pump output control 20, simultaneously the output control valve 11 on the pipeline 9 is opened, and the input control valve 10 of the pipeline 9a on the composite additive jar 3 opened, acetone, ether, the trimethyl carbinol, cerous nitrate, Virahol is from the additive tank 1 pipeline 9i that flows through, and the pressure by additive pump 18 is with acetone again, ether, the trimethyl carbinol, cerous nitrate, it is standby that Virahol exports composite additive jar 3 to through pipeline 9 and 9a;
3) jar 1 is added in the gasoline input, cover sealing cover 17, additive pump input control valve 19 on the opening conduits 9i and additive pump output control 20, simultaneously the output control valve 11 on the pipeline 9 is opened, and the input control valve 10 of the pipeline 9a on the gasoline tank 4 opened, gasoline is from the additive tank 1 pipeline 9i that flows through, and to export gasoline to gasoline tank 4 through pipeline 9 and 9a standby for the pressure by additive pump 18 again;
4) jar 1 is added in the combined additive input, cover sealing cover 17, additive pump input control valve 19 on the opening conduits 9i and additive pump output control 20, simultaneously the output control valve 11 on the pipeline 9 is opened, and the input control valve 10 of the pipeline 9a on the gasoline tank 4 opened, combined additive is from the additive tank 1 pipeline 9i that flows through, and to export combined additive to gasoline tank 4 through pipeline 9 and 9a standby for the pressure by additive pump 18 again;
5) open methanol tank 2 respectively, composite additive jar 3, output control valve 11 on gasoline tank 4 and the combined additive jar 5 lower channel 9b, with methyl alcohol, composite additive, gasoline and combined additive export pipeline 9c to, again with the pressure pump 21 at pipeline 9c two ends, pressure pump input control valve 22 on 24,22 and pressure pump output control valve 23,26 open, overhead control valve 12 on the opening conduits 9d and pipeline 9e one end connect the input control valve 10 of mixing tank 13 upper ends simultaneously, close the input control valve 10 of standby mixing tank 7 upper ends, methyl alcohol, composite additive, gasoline and combined additive are respectively through pipeline 9b flow ipe 9c, by pressure pump 21,24 pressure is with methyl alcohol, composite additive, gasoline and combined additive are through pipeline 9j, 9k, 9c, in 9d and the pipeline 9e input mixing tank 6.
6) the circulating pressure oil pump input control valve 15 and the circulating pressure oil pump output control valve 16 that will connect on the pipeline 9l of mixing tank 6 opened, compounded oil in the mixing tank 6 flow through pipeline 9l and circulation pressure oil pump 14 and compounded oil is sprayed in the mixing tank 6 by nozzle 13, carried out self-circulation 20-30 minute, the oil tank oil level of controlling mixing tank 6 simultaneously is at normal value, promptly become the methyl alcohol compounded oil, last opening conduits 9f connects the output control valve 11 of mixing tank 6 one ends and the input control valve 10 on the pipeline 9g, close pipeline 9f and connect the output control valve 11 of standby mixing tank 7 one ends, the methyl alcohol compounded oil in the mixing tank 6 exports product tank 8 to through pipeline 9f and pipeline 9g and stores.
Another preparation method of methanol composite gasoline of the present invention is by following steps:
1) methyl alcohol is imported additive tank 1, cover sealing cover 17, additive pump input control valve 19 on the opening conduits 9i and additive pump output control 20, simultaneously the output control valve 11 on the pipeline 9 is opened, and the input control valve 10 of the pipeline 9a on the methanol tank 2 opened, methyl alcohol is from the additive tank 1 pipeline 9i that flows through, and to export methyl alcohol to methanol tank 2 through pipeline 9 and 9a standby for the pressure by additive pump 18 again;
2) with acetone, ether, the trimethyl carbinol, cerous nitrate, Virahol input additive tank 1, cover sealing cover 17, additive pump input control valve 19 on the opening conduits 9i and additive pump output control 20, simultaneously the output control valve 11 on the pipeline 9 is opened, and the input control valve 10 of the pipeline 9a on the composite additive jar 3 opened, acetone, ether, the trimethyl carbinol, cerous nitrate, Virahol is from the additive tank 1 pipeline 9i that flows through, and the pressure by additive pump 18 is with acetone again, ether, the trimethyl carbinol, cerous nitrate, it is standby that Virahol exports composite additive jar 3 to through pipeline 9 and 9a;
3) jar 1 is added in the gasoline input, cover sealing cover 17, additive pump input control valve 19 on the opening conduits 9i and additive pump output control 20, simultaneously the output control valve 11 on the pipeline 9 is opened, and the input control valve 10 of the pipeline 9a on the gasoline tank 4 opened, gasoline is from the additive tank 1 pipeline 9i that flows through, and to export gasoline to gasoline tank 4 through pipeline 9 and 9a standby for the pressure by additive pump 18 again;
4) jar 1 is added in the combined additive input, cover sealing cover 17, additive pump input control valve 19 on the opening conduits 9i and additive pump output control 20, simultaneously the output control valve 11 on the pipeline 9 is opened, and the input control valve 10 of the pipeline 9a on the gasoline tank 4 opened, combined additive is from the additive tank 1 pipeline 9i that flows through, and to export combined additive to gasoline tank 4 through pipeline 9 and 9a standby for the pressure by additive pump 18 again;
5) open methanol tank 2 respectively, composite additive jar 3, output control valve 11 on gasoline tank 4 and the combined additive jar 5 lower channel 9b, with methyl alcohol, composite additive, gasoline and combined additive export pipeline 9c to, again with the pressure pump 21 at pipeline 9c two ends, pressure pump input control valve 22 on 24,25 and pressure pump output control valve 23,26 open, the input control valve 10 that overhead control valve 12 on the while opening conduits 9d and pipeline 9e one end connect standby mixing tank 7 upper ends, close the input control valve 10 of mixing tank 6 upper ends, methyl alcohol, composite additive, gasoline and combined additive are respectively through pipeline 9b flow ipe 9c, by pressure pump 21,24 pressure is with methyl alcohol, composite additive, gasoline and combined additive are through pipeline 9j, 9k, 9c, 9d and pipeline 9e import in the standby mixing tank 7;
6) the circulating pressure oil pump input control valve 15a and the circulating pressure oil pump output control valve 16a that will connect on the pipeline 9l of standby mixing tank 7 opens, compounded oil flow ipe 9l in the standby mixing tank 6, pressure by circulation pressure oil pump 14a is in nozzle 13a sprays into compounded oil standby mixing tank 7, carried out self-circulation 20-30 minute, the oil tank oil level of controlling standby mixing tank 7 simultaneously is at normal value, promptly become the methyl alcohol compounded oil, last opening conduits 9f connects the output control valve 11 of standby mixing tank 7 one ends and the input control valve 10 on the pipeline 9g, close the output control valve 11 of pipeline 9f connection mixing tank 6 one ends, the methyl alcohol compounded oil in the standby mixing tank 7 exports product tank 8 storages to through pipeline 9f and pipeline 9g.
Be 30 minutes described above-mentioned three kinds of preparation methods' cycling time.
Methanol composite gasoline of the present invention can solve mechanical property, dynamic performance, safety performance, starting performance, anti-knocking property, oxidation-resistance, the erosion resistance of automobile, reduce discharging, environment purification, reduction oil consumption, swelling property, engine oil filter screen to rubber stop up, carbon deposit, work-ing life etc. a series of problems, and thoroughly solved having a strong impact on that petrochemical industry gasoline mixing use is caused, use the methanol composite gasoline of this kind environment-friendly type to reduce cost.The technology of the present invention equipment is simple, less investment, speed is fast, the cycle is short, the high operability of economic benefit is stronger.The present invention all adopts automatic routine control in system operation, save a large amount of human and material resources, financial resources, thereby reduced comprehensive cost cost and closed production run, has improved economy and safe reliability more.
Description of drawings
Fig. 1 is preparation method's of the present invention system architecture synoptic diagram.
Wherein:
1 is additive tank, and 2 is methanol tank, and 3 is the composite additive jar, 4 is gasoline tank, and 5 is the combined additive jar, and 6 is mixing tank, 7 is standby mixing tank, 8 is product tank, 9,9a, 9b, 9c, 9d, 9e, 9f, 9g, 9h, 9i, 9j, 9k, 9l, 9m is a pipeline, and 10 is input control valve, 11 are the output control valve, 12 are overhead control valve, 13,13a is a nozzle, 14,14a is the circulating pressure oil pump, 15,15a is a circulating pressure oil pump input control valve, 16,16a is circulating pressure oil pump output control valve, and 17 is sealing cover, and 18 is additive pump, 19 is the additive pump input control valve, 20 are additive pump output control valve, 21,24 is pressure pump, 22,25 is the pressure pump input control valve, 23,26 are pressure pump output control valve, 27 is Send out pump, and 28 is the Send out pump input control valve, and 29 are Send out pump output control valve.
Following experimental example and embodiment are used to further specify but are not limited to the present invention.
Experimental example 1
The present invention carries out the actual performance test in scene once more at Shandong Shengli Oil Field Dongying refinery, raw material is provided by refinery fully, more any test was significantly improved than in the past through test-results proof general data octane value, and other data all are lower than GB white gasoline 93#, 97# prescribed value following a lot (seeing the following form).
Shengli Oil Field company limited general petrochemical works
The petroleum products product certificate
| Name of product | ||||
| Methanol composite gasoline | ||||
| Project | Quality index | Actual | ||
| Research octane number (RON) (RON) is not less than | 94.3 | |||
| Antiknock is carried number (RON+MON)/2 and is not less than | ||||
| Lead content g/L is not more than | 0.005 | 0.007 | ||
| Boiling range: 10% vaporization temperature ℃ is not higher than | 70 | 65 | ||
| 50% vaporization temperature ℃ is not higher than | 120 | 117 | ||
| 90% vaporization temperature ℃ is not higher than | 190 | 186 | ||
| Final boiling point ℃ is not higher than | 205 | 197 | ||
| Residual quantity V/V % is not more than | 2 | 1.3 | ||
| The full vapour pressure Kpa that closes was not more than from September 16 to March on the 15th | 88 | 72 | ||
| Be not more than in 15th from March 16 to September | 74 | |||
| Existent gum mg/100ml is not more than | 5 | 1 | ||
| Inductive phase, min was not less than | 480 | 480 | ||
| Sulphur content % (m/m) is not more than | 0.08 | 0.003 | ||
| Mercaptan (need satisfy one of following requirement) | The doctor test | By | By | |
| (% (m/m) is not more than mercaptan sulfur content | 0.001 | 0.0001 | ||
| (50 ℃, 3h) level is not more than in copper corrosion | 1 | 1 | ||
| Water soluble acid or alkali | Do not have | Do not have | ||
| Mechanical impurity and moisture | Do not have | Do not have | ||
| Benzene content % (V/V) is not more than | 205 | 0.8 | ||
| Aromaticity content % (V/V) is not more than | 40 | 31 | ||
| Olefin(e) centent % (V/V) is not more than | 35 | 14 | ||
| Density (20 ℃) kg/m 3 | Actual measurement | 0.717 | ||
| Product judging criterion GB17930-1999 | ||||
Experimental example 2
It is that a difficult problem and dynamic performance, the climbing strength that thoroughly solves clogging of oil screen, carbon deposit improves significantly, the environmental protection exhaust emissions is lower than Europe IV standard that the present invention does the advantage that the various road surfaces of 1000km road test compares with existing methanol gasoline technical feature through Buick automobile 3.0 steam discharges.
Following embodiment all can realize the described effect of above-mentioned experimental example.
Embodiment
Embodiment 1:
Methyl alcohol 35L gasoline 40L acetone 4L
Ether 7L trimethyl carbinol 4L cerous nitrate 2L
Virahol 2L combined additive 6L;
Wherein the component of combined additive is: active zinc flower 2.6L, isopropyl nitrate 1.5L, triamine 1.5L, dimethylbenzene 0.08L, hydrogen peroxidase 10 .32L.
1) methyl alcohol is imported additive tank 1, cover sealing cover 17, additive pump input control valve 19 on the opening conduits 9i and additive pump output control 20, simultaneously the output control valve 11 on the pipeline 9 is opened, and the input control valve 10 of the pipeline 9a on the methanol tank 2 opened, methyl alcohol is from the additive tank 1 pipeline 9i that flows through, and to export methyl alcohol to methanol tank 2 through pipeline 9 and 9a standby for the pressure by additive pump 18 again;
2) with acetone, ether, the trimethyl carbinol, cerous nitrate, Virahol input additive tank 1, cover sealing cover 17, additive pump input control valve 19 on the opening conduits 9i and additive pump output control 20, simultaneously the output control valve 11 on the pipeline 9 is opened, and the input control valve 10 of the pipeline 9a on the composite additive jar 3 opened, acetone, ether, the trimethyl carbinol, cerous nitrate, Virahol is from the additive tank 1 pipeline 9i that flows through, and the pressure by additive pump 18 is with acetone again, ether, the trimethyl carbinol, cerous nitrate, it is standby that Virahol exports composite additive jar 3 to through pipeline 9 and 9a;
3) with the homemade petrochemical industry gasoline input of 90# additive tank 1, cover sealing cover 17, additive pump input control valve 19 on the opening conduits 9i and additive pump output control 20, simultaneously the output control valve 11 on the pipeline 9 is opened, and the input control valve 10 of the pipeline 9a on the gasoline tank 4 opened, the homemade petrochemical industry gasoline of 90# is from the additive tank 1 pipeline 9i that flows through, and to export the homemade petrochemical industry gasoline of 90# to gasoline tank 4 through pipeline 9 and 9a standby for the pressure by additive pump 18 again;
4) combined additive is imported additive tank 1, cover sealing cover 17, additive pump input control valve 19 on the opening conduits 9i and additive pump output control 20, simultaneously the output control valve 11 on the pipeline 9 is opened, and the input control valve 10 of the pipeline 9a on the gasoline tank 4 opened, combined additive is from the additive tank 1 pipeline 9i that flows through, and to export combined additive to gasoline tank 4 through pipeline 9 and 9a standby for the pressure by additive pump 18 again;
5) open methanol tank 2 respectively, composite additive jar 3, output control valve 11 on gasoline tank 4 and the combined additive jar 5 lower channel 9b, with methyl alcohol, composite additive, gasoline and combined additive export pipeline 9c to, again with the pressure pump 21 at pipeline 9c two ends, pressure pump input control valve 22 on 24,25 and pressure pump output control valve 23,26 open, overhead control valve 12 on the opening conduits 9d and pipeline 9e one end connect the input control valve 10 of mixing tank 6 upper ends simultaneously, close the input control valve 10 of standby mixing tank 7 upper ends, methyl alcohol, composite additive, gasoline and combined additive are respectively through pipeline 9b flow ipe 9c, by pressure pump 21,24 pressure is with methyl alcohol, composite additive, gasoline and combined additive are through pipeline 9j, 9k, 9c, in 9d and the pipeline 9e input mixing tank 6.
6) the circulating pressure oil pump input control valve 15 and the circulating pressure oil pump output control valve 16 that will connect on the pipeline 9l of mixing tank 6 opened, compounded oil in the mixing tank 6 flow through pipeline 9l and circulation pressure oil pump 14 and compounded oil is sprayed in the mixing tank 6 by nozzle 13, carried out self-circulation 30 minutes, the oil tank oil level of controlling mixing tank 6 simultaneously is at normal value, promptly become the methyl alcohol compounded oil, last opening conduits 9f connects the output control valve 11 of mixing tank 6 one ends and the input control valve 10 on the pipeline 9g, close pipeline 9f and connect the output control valve 11 of standby mixing tank 7 one ends, methyl alcohol compounded oil in the mixing tank 6 exports product tank 8 storages to through pipeline 9f and pipeline 9g, Send out pump input control valve 28 on the opening conduits 9h and Send out pump are exported control valve 29, by the pressure of Send out pump 27 methanol composite gasoline of storing in the product tank 8 are exported through pipeline 9h to get final product.
Embodiment 2:
The homemade petrochemical industry gasoline of methyl alcohol 35L 90# 38L
Acetone 3L ether 4.5L
Trimethyl carbinol 2.5L cerous nitrate 3L
Virahol 3L combined additive 5.5L;
Wherein the component of combined additive is: active zinc flower 2.2L, isopropyl nitrate 1.35L, triamine 1.59L, dimethylbenzene 0.06L, hydrogen peroxidase 10 .3L.
Mixing tank is injected in methyl alcohol, the homemade petrochemical industry gasoline of 90#, acetone, ether, the trimethyl carbinol, cerous nitrate, Virahol and combined additive convection current from different directions simultaneously, when each ingredients substance all in proportion the filling finish after, all inject mixing tank again with oil pump, in jar, use circulating oil pump to carry out mixed cycle 30 minutes, promptly prepare with oil pump injection product tank at last and finish.
Embodiment 3:
The homemade petrochemical industry gasoline of methyl alcohol 35L 90# 38L
Acetone 3L ether 4.5L
Trimethyl carbinol 2.5L cerous nitrate 3L
Virahol 3L combined additive 5.5L;
Wherein the component of combined additive is: active zinc flower 2.2L, isopropyl nitrate 1.35L, triamine 1.59L, dimethylbenzene 0.06L, hydrogen peroxidase 10 .3L.
1) methyl alcohol is imported additive tank 1, cover sealing cover 17, additive pump input control valve 19 on the opening conduits 9i and additive pump output control 20, simultaneously the output control valve 11 on the pipeline 9 is opened, and the input control valve 10 of the pipeline 9a on the methanol tank 2 opened, methyl alcohol is from the additive tank 1 pipeline 9i that flows through, and to export methyl alcohol to methanol tank 2 through pipeline 9 and 9a standby for the pressure by additive pump 18 again;
2) with acetone, ether, the trimethyl carbinol, cerous nitrate, Virahol input additive tank 1, cover sealing cover 17, additive pump input control valve 19 on the opening conduits 9i and additive pump output control 20, simultaneously the output control valve 11 on the pipeline 9 is opened, and the input control valve 10 of the pipeline 9a on the composite additive jar 3 opened, acetone, ether, the trimethyl carbinol, cerous nitrate, Virahol is from the additive tank 1 pipeline 9i that flows through, and the pressure by additive pump 18 is with acetone again, ether, the trimethyl carbinol, cerous nitrate, it is standby that Virahol exports composite additive jar 3 to through pipeline 9 and 9a;
3) with the homemade petrochemical industry gasoline input of 90# additive tank 1, cover sealing cover 17, additive pump input control valve 19 on the opening conduits 9i and additive pump output control 20, simultaneously the output control valve 11 on the pipeline 9 is opened, and the input control valve 10 of the pipeline 9a on the gasoline tank 4 opened, the homemade petrochemical industry gasoline of 90# is from the additive tank 1 pipeline 9i that flows through, and to export the homemade petrochemical industry gasoline of 90# to gasoline tank 4 through pipeline 9 and 9a standby for the pressure by additive pump 18 again;
4) combined additive is imported additive tank 1, cover sealing cover 17, additive pump input control valve 19 on the opening conduits 9i and additive pump output control 20, simultaneously the output control valve 11 on the pipeline 9 is opened, and the input control valve 10 of the pipeline 9a on the gasoline tank 4 opened, combined additive is from the additive tank 1 pipeline 9i that flows through, and to export combined additive to gasoline tank 4 through pipeline 9 and 9a standby for the pressure by additive pump 18 again;
5) open methanol tank 2 respectively, composite additive jar 3, output control valve 11 on gasoline tank 4 and the combined additive jar 5 lower channel 9b, with methyl alcohol, composite additive, gasoline and combined additive export pipeline 9c to, again with the pressure pump 21 at pipeline 9c two ends, pressure pump input control valve 22 on 24,25 and pressure pump output control valve 23,26 open, overhead control valve 12 on the opening conduits 9d and pipeline 9e one end connect the input control valve 10 of mixing tank 6 upper ends simultaneously, close the input control valve 10 of standby mixing tank 7 upper ends, methyl alcohol, composite additive, gasoline and combined additive are respectively through pipeline 9b flow ipe 9c, by pressure pump 21,24 pressure is with methyl alcohol, composite additive, gasoline and combined additive are through pipeline 9j, 9k, 9c, in 9d and the pipeline 9e input mixing tank 6.
6) the circulating pressure oil pump input control valve 15 and the circulating pressure oil pump output control valve 16 that will connect on the pipeline 9l of mixing tank 6 opened, compounded oil in the mixing tank 6 flow through pipeline 9l and circulation pressure oil pump 14 and compounded oil is sprayed in the mixing tank 6 by nozzle 13, carried out self-circulation 25 minutes, the oil tank oil level of controlling mixing tank 6 simultaneously is at normal value, promptly become the methyl alcohol compounded oil, last opening conduits 9f connects the output control valve 11 of mixing tank 6 one ends and the input control valve 10 on the pipeline 9g, close pipeline 9f and connect the output control valve 11 of standby mixing tank 7 one ends, methyl alcohol compounded oil in the mixing tank 6 exports product tank 8 storages to through pipeline 9f and pipeline 9g, Send out pump input control valve 28 on the opening conduits 9h and Send out pump are exported control valve 29, by the pressure of Send out pump 27 methanol composite gasoline of storing in the product tank 8 are exported through pipeline 9h to get final product.
Embodiment 4:
The homemade petrochemical industry gasoline of methyl alcohol 15L 90# 60L
Acetone 4.5L ether 1.5L
Trimethyl carbinol 1.5L cerous nitrate 4.5L
Virahol 4.5L combined additive 1.5L.
Wherein the component of combined additive is: active zinc flower 0.5L, isopropyl nitrate 0.5L, triamine 0.2L, dimethylbenzene 0.03L, hydrogen peroxidase 10 .27L.
Wherein the component of combined additive is: active zinc flower 2.2L, isopropyl nitrate 1.35L, triamine 1.59L, dimethylbenzene 0.06L, hydrogen peroxidase 10 .3L.
Mixing tank is injected in methyl alcohol, the homemade petrochemical industry gasoline of 90#, acetone, ether, the trimethyl carbinol, cerous nitrate, Virahol and combined additive convection current from different directions simultaneously, when each ingredients substance all in proportion the filling finish after, all inject mixing tank again with oil pump, in jar, use circulating oil pump to carry out mixed cycle 25 minutes, promptly prepare with oil pump injection product tank at last and finish.
Embodiment 5:
Methyl alcohol 35L gasoline 40L acetone 4L
Ether 7L trimethyl carbinol 4L cerous nitrate 2L
Virahol 2L combined additive 6L;
Wherein the component of combined additive is: active zinc flower 2.6L, isopropyl nitrate 1.5L, triamine 1.5L, dimethylbenzene 0.08L, hydrogen peroxidase 10 .32L.
1) methyl alcohol is imported additive tank 1, cover sealing cover 17, additive pump input control valve 19 on the opening conduits 9i and additive pump output control 20, simultaneously the output control valve 11 on the pipeline 9 is opened, and the input control valve 10 of the pipeline 9a on the methanol tank 2 opened, methyl alcohol is from the additive tank 1 pipeline 9i that flows through, and to export methyl alcohol to methanol tank 2 through pipeline 9 and 9a standby for the pressure by additive pump 18 again;
2) with acetone, ether, the trimethyl carbinol, cerous nitrate, jar 1 is added in the Virahol input, cover sealing cover 17, additive pump input control valve 19 on the opening conduits 9i and additive pump output control 20, simultaneously the output control valve 11 on the pipeline 9 is opened, and the input control valve 10 of the pipeline 9a on the composite additive jar 3 opened, acetone, ether, the trimethyl carbinol, cerous nitrate, Virahol is from the additive tank 1 pipeline 9i that flows through, and the pressure by additive pump 18 is with acetone again, ether, the trimethyl carbinol, cerous nitrate, it is standby that Virahol exports composite additive jar 3 to through pipeline 9 and 9a;
3) jar 1 is added in the homemade petrochemical industry gasoline input of 90#, cover sealing cover 17, additive pump input control valve 19 on the opening conduits 9i and additive pump output control 20, simultaneously the output control valve 11 on the pipeline 9 is opened, and the input control valve 10 of the pipeline 9a on the gasoline tank 4 opened, the homemade petrochemical industry gasoline of 90# is from the additive tank 1 pipeline 9i that flows through, and to export the homemade petrochemical industry gasoline of 90# to gasoline tank 4 through pipeline 9 and 9a standby for the pressure by additive pump 18 again;
4) jar 1 is added in the combined additive input, cover sealing cover 17, additive pump input control valve 19 on the opening conduits 9i and additive pump output control 20, simultaneously the output control valve 11 on the pipeline 9 is opened, and the input control valve 10 of the pipeline 9a on the gasoline tank 4 opened, combined additive is from the additive tank 1 pipeline 9i that flows through, and to export combined additive to gasoline tank 4 through pipeline 9 and 9a standby for the pressure by additive pump 18 again;
5) open methanol tank 2 respectively, composite additive jar 3, output control valve 11 on gasoline tank 4 and the combined additive jar 5 lower channel 9b, with methyl alcohol, composite additive, gasoline and combined additive export pipeline 9c to, again with the pressure pump 21 at pipeline 9c two ends, pressure pump input control valve 22 on 24,25 and pressure pump output control valve 23,26 open, the input control valve 10 that overhead control valve 12 on the while opening conduits 9d and pipeline 9e one end connect standby mixing tank 7 upper ends, close the input control valve 10 of mixing tank 6 upper ends, methyl alcohol, composite additive, gasoline and combined additive are respectively through pipeline 9b flow ipe 9c, by pressure pump 21,24 pressure is with methyl alcohol, composite additive, gasoline and combined additive are through pipeline 9j, 9k, 9c, 9d and pipeline 9e import in the standby mixing tank 7;
6) the circulating pressure oil pump input control valve 15a and the circulating pressure oil pump output control valve 16a that will connect on the pipeline 9l of standby mixing tank 7 opens, compounded oil flow ipe 9l in the standby mixing tank 6, pressure by circulation pressure oil pump 14a is in nozzle 13a sprays into compounded oil standby mixing tank 7, carried out self-circulation 30 minutes, the oil tank oil level of controlling standby mixing tank 7 simultaneously is at normal value, promptly become the methyl alcohol compounded oil, last opening conduits 9f connects the output control valve 11 of standby mixing tank 7 one ends and the input control valve 10 on the pipeline 9g, close pipeline 9f and connect the output control valve 11 of mixing tank 6 one ends, the methyl alcohol compounded oil in the standby mixing tank 7 exports product tank 8 to through pipeline 9f and pipeline 9g and stores and get final product.
Embodiment 6:
The homemade petrochemical industry gasoline of methyl alcohol 45L 90# 25L
Acetone 2L ether 5L
Trimethyl carbinol 1.5L cerous nitrate 2L
Virahol 2L combined additive 7L.
Wherein the component of combined additive is: active zinc flower 3L, isopropyl nitrate 2L, triamine 1.5L, dimethylbenzene 0.08L, hydrogen peroxidase 10 .42L.
1) methyl alcohol is imported additive tank 1, cover sealing cover 17, additive pump input control valve 19 on the opening conduits 9i and additive pump output control 20, simultaneously the output control valve 11 on the pipeline 9 is opened, and the input control valve 10 of the pipeline 9a on the methanol tank 2 opened, methyl alcohol is from the additive tank 1 pipeline 9i that flows through, and to export methyl alcohol to methanol tank 2 through pipeline 9 and 9a standby for the pressure by additive pump 18 again;
2) with acetone, ether, the trimethyl carbinol, cerous nitrate, jar 1 is added in the Virahol input, cover sealing cover 17, additive pump input control valve 19 on the opening conduits 9i and additive pump output control 20, simultaneously the output control valve 11 on the pipeline 9 is opened, and the input control valve 10 of the pipeline 9a on the composite additive jar 3 opened, acetone, ether, the trimethyl carbinol, cerous nitrate, Virahol is from the additive tank 1 pipeline 9i that flows through, and the pressure by additive pump 18 is with acetone again, ether, the trimethyl carbinol, cerous nitrate, it is standby that Virahol exports composite additive jar 3 to through pipeline 9 and 9a;
3) jar 1 is added in the homemade petrochemical industry gasoline input of 90#, cover sealing cover 17, additive pump input control valve 19 on the opening conduits 9i and additive pump output control 20, simultaneously the output control valve 11 on the pipeline 9 is opened, and the input control valve 10 of the pipeline 9a on the gasoline tank 4 opened, the homemade petrochemical industry gasoline of 90# is from the additive tank 1 pipeline 9i that flows through, and to export the homemade petrochemical industry gasoline of 90# to gasoline tank 4 through pipeline 9 and 9a standby for the pressure by additive pump 18 again;
4) jar 1 is added in the combined additive input, cover sealing cover 17, additive pump input control valve 19 on the opening conduits 9i and additive pump output control 20, simultaneously the output control valve 11 on the pipeline 9 is opened, and the input control valve 10 of the pipeline 9a on the gasoline tank 4 opened, combined additive is from the additive tank 1 pipeline 9i that flows through, and to export combined additive to gasoline tank 4 through pipeline 9 and 9a standby for the pressure by additive pump 18 again;
5) open methanol tank 2 respectively, composite additive jar 3, output control valve 11 on gasoline tank 4 and the combined additive jar 5 lower channel 9b, with methyl alcohol, composite additive, gasoline and combined additive export pipeline 9c to, again with the pressure pump 21 at pipeline 9c two ends, pressure pump input control valve 22 on 24,25 and pressure pump output control valve 23,26 open, the input control valve 10 that overhead control valve 12 on the while opening conduits 9d and pipeline 9e one end connect standby mixing tank 7 upper ends, close the input control valve 10 of mixing tank 6 upper ends, methyl alcohol, composite additive, gasoline and combined additive are respectively through pipeline 9b flow ipe 9c, by pressure pump 21,24 pressure is with methyl alcohol, composite additive, gasoline and combined additive are through pipeline 9j, 9k, 9c, 9d and pipeline 9e import in the standby mixing tank 7;
6) the circulating pressure oil pump input control valve 15a and the circulating pressure oil pump output control valve 16a that will connect on the pipeline 9l of standby mixing tank 7 opens, compounded oil flow ipe 9l in the standby mixing tank 6, pressure by circulation pressure oil pump 14a is in nozzle 13a sprays into compounded oil standby mixing tank 7, carried out self-circulation 25 minutes, the oil tank oil level of controlling standby mixing tank 7 simultaneously is at normal value, promptly become the methyl alcohol compounded oil, last opening conduits 9f connects the output control valve 11 of standby mixing tank 7 one ends and the input control valve 10 on the pipeline 9g, close pipeline 9f and connect the output control valve 11 of mixing tank 6 one ends, the methyl alcohol compounded oil in the standby mixing tank 7 exports product tank 8 to through pipeline 9f and pipeline 9g and stores and get final product.
Claims (10)
1. methanol composite gasoline is characterized in that the component of this methanol composite gasoline is:
Methyl alcohol 10-60 weight part gasoline 10-65 weight part
Acetone 1-5 weight part ether 1-8 weight part
Trimethyl carbinol 1-4 weight part cerous nitrate 1-5 weight part
Virahol 1-5 weight part combined additive 1-10 weight part;
Wherein the component of combined additive is: active zinc flower 0.4-4 weight part, isopropyl nitrate 0.3-2.4 weight part, triamine 0.18-3 weight part, dimethylbenzene 0.02-0.1 weight part, hydrogen peroxidase 10 .1-0.5 weight part.
2. methanol composite gasoline according to claim 1 is characterized in that the component of this methanol composite gasoline is:
Methyl alcohol 35 weight part gasoline 40 weight part acetone 4 weight parts
The ether 7 weight part trimethyl carbinols 4 weight part cerous nitrates 2 weight parts
Virahol 2 weight part combined additives 6;
Wherein the component of combined additive is: active zinc flower 2.6 weight parts, isopropyl nitrate 1.5 weight parts, triamine 1.5 weight parts, dimethylbenzene 0.08 weight part, hydrogen peroxidase 10 .32 weight part.
3. methanol composite gasoline according to claim 1 is characterized in that the component of this methanol composite gasoline is:
Methyl alcohol 35 weight part gasoline 38 weight parts
Acetone 3 weight part ether 4.5 weight parts
The trimethyl carbinol 2.5 weight part cerous nitrates 3 weight parts
Virahol 3 weight part combined additives 5.5 weight parts;
Wherein the component of combined additive is: active zinc flower 2.2 weight parts, isopropyl nitrate 1.35 weight parts, triamine 1.59 weight parts, dimethylbenzene 0.06 weight part, hydrogen peroxidase 10 .3 weight part.
4. methanol composite gasoline according to claim 1 is characterized in that the component of this methanol composite gasoline is:
Methyl alcohol 15 weight part gasoline 60 weight parts
Acetone 4.5 weight part ether 1.5 weight parts
The trimethyl carbinol 1.5 weight part cerous nitrates 4.5 weight parts
Virahol 4.5 weight part combined additives 1.5 weight parts.
Wherein the component of combined additive is: active zinc flower 0.5 weight part, isopropyl nitrate 0.5 weight part, triamine 0.2 weight part, dimethylbenzene 0.03 weight part, hydrogen peroxidase 10 .27 weight part.
5. methanol composite gasoline according to claim 1 is characterized in that the component of this methanol composite gasoline is:
Methyl alcohol 45 weight part gasoline 25 weight parts
Acetone 2 weight part ether 5 weight parts
The trimethyl carbinol 1.5 weight part cerous nitrates 2 weight parts
Virahol 2 weight part combined additives 7 weight parts.
Wherein the component of combined additive is: active zinc flower 3 weight parts, isopropyl nitrate 2 weight parts, triamine 1.5 weight parts, dimethylbenzene 0.08 weight part, hydrogen peroxidase 10 .42 weight part.
6. according to the described methanol composite gasoline of one of claim 1-5, it is characterized in that described gasoline is the homemade petrochemical industry gasoline of 90#, the homemade petrochemical industry gasoline of 93# or the homemade petrochemical industry gasoline of 97#.
7. according to the preparation method of one of claim 1-6 described methanol composite gasoline, it is characterized in that this method is: methyl alcohol, gasoline, acetone, ether, the trimethyl carbinol, cerous nitrate, Virahol and combined additive are injected mixing tank simultaneously by the convection current from different directions of Different Weight part, when each ingredients substance all in proportion the filling finish after, all inject mixing tank again with oil pump, in jar, use circulating oil pump to carry out mixed cycle 20-30 minute, promptly prepare with oil pump injection product tank at last and finish.
8. according to the preparation method of one of claim 1-6 described methanol composite gasoline, it is characterized in that this preparation method comprises the steps:
Methyl alcohol is imported additive tank (1), cover sealing cover (17), additive pump input control valve (19) on the opening conduits (9i) and additive pump output control (20), simultaneously the output control valve (11) on the pipeline (9) is opened, and the input control valve (10) of the pipeline (9a) on the methanol tank (2) opened, methyl alcohol is from additive tank (1) pipeline (9i) of flowing through, and through pipeline (9) and (9a) to export methyl alcohol to methanol tank (2) standby for the pressure by additive pump (18) again;
With acetone, ether, the trimethyl carbinol, cerous nitrate, Virahol input additive tank (1), cover sealing cover (17), additive pump input control valve (19) on the opening conduits (9i) and additive pump output control (20), simultaneously the output control valve (11) on the pipeline (9) is opened, and the input control valve (10) of the pipeline (9a) on the composite additive jar (3) opened, acetone, ether, the trimethyl carbinol, cerous nitrate, Virahol is from additive tank (1) pipeline (9i) of flowing through, and the pressure by additive pump (18) is with acetone again, ether, the trimethyl carbinol, cerous nitrate, Virahol is through pipeline (9) and (9a) to export composite additive jar (3) to standby;
Gasoline is imported additive tank (1), cover sealing cover (17), additive pump input control valve (19) on the opening conduits (9i) and additive pump output control (20), simultaneously the output control valve (11) on the pipeline (9) is opened, and the input control valve (10) of the pipeline (9a) on the gasoline tank (4) opened, gasoline is from additive tank (1) pipeline (9i) of flowing through, and through pipeline (9) and (9a) to export gasoline to gasoline tank (4) standby for the pressure by additive pump (18) again;
Combined additive is imported additive tank (1), cover sealing cover (17), additive pump input control valve (19) on the opening conduits (9i) and additive pump output control (20), simultaneously the output control valve (11) on the pipeline (9) is opened, and the input control valve (10) of the pipeline (9a) on the gasoline tank (4) opened, combined additive is from additive tank (1) pipeline (9i) of flowing through, and through pipeline (9) and (9a) to export combined additive to gasoline tank (4) standby for the pressure by additive pump (18) again;
Open methanol tank (2) respectively, composite additive jar (3), output control valve (11) on gasoline tank (4) and combined additive jar (5) lower channel (9b), with methyl alcohol, composite additive, gasoline and combined additive export pipeline (9c) to, again with the pressure pump (21 at pipeline (9c) two ends, 24) the pressure pump input control valve (22 on, 25) and pressure pump output control valve (23,26) open, overhead control valve (12) on the opening conduits (9d) and pipeline (9e) end connect the input control valve (10) of mixing tank (6) upper end simultaneously, close the input control valve (10) of standby mixing tank (7) upper end, methyl alcohol, composite additive, gasoline and combined additive are respectively through pipeline (9b) flow ipe (9c), by pressure pump (21,24) pressure is with methyl alcohol, composite additive, gasoline and combined additive are through pipeline (9j, 9k, 9c, 9d) and in pipeline (9e) the input mixing tank (6);
The circulating pressure oil pump input control valve (15) and the circulating pressure oil pump output control valve (16) that will connect on the pipeline (9l) of mixing tank (6) are opened, the pressure of compounded oil flow ipe (9l) in the mixing tank (6) by circulation pressure oil pump (14) is in nozzle (13) sprays into compounded oil mixing tank (6), carried out self-circulation 20-30 minute, the oil tank oil level of controlling mixing tank (6) simultaneously is at normal value, promptly become the methyl alcohol compounded oil, last opening conduits (9f) connects the output control valve (11) of mixing tank (6) one ends and the input control valve (10) on the pipeline (9g), close pipeline (9f) and connect the output control valve (11) of standby mixing tank (7) one ends, the methyl alcohol compounded oil in the mixing tank (6) exports product tank (8) to through pipeline (9f) and pipeline (9g) and stores and get final product.
9. according to the preparation method of one of claim 1-6 described methanol composite gasoline, it is characterized in that this method comprises the steps:
Methyl alcohol is imported additive tank (1), cover sealing cover (17), additive pump input control valve (19) on the opening conduits (9i) and additive pump output control (20), simultaneously the output control valve (11) on the pipeline (9) is opened, and the input control valve (10) of the pipeline (9a) on the methanol tank (2) opened, methyl alcohol is from additive tank (1) pipeline (9i) of flowing through, and through pipeline (9) and (9a) to export methyl alcohol to methanol tank (2) standby for the pressure by additive pump (18) again;
With acetone, ether, the trimethyl carbinol, cerous nitrate, jar (1) is added in the Virahol input, cover sealing cover (17), additive pump input control valve (19) on the opening conduits (9i) and additive pump output control (20), simultaneously the output control valve (11) on the pipeline (9) is opened, and the input control valve (10) of the pipeline (9a) on the composite additive jar (3) opened, acetone, ether, the trimethyl carbinol, cerous nitrate, Virahol is from additive tank (1) pipeline (9i) of flowing through, and the pressure by additive pump (18) is with acetone again, ether, the trimethyl carbinol, cerous nitrate, Virahol is through pipeline (9) and (9a) to export composite additive jar (3) to standby;
Jar (1) is added in the homemade petrochemical industry gasoline input of 90#, cover sealing cover (17), additive pump input control valve (19) on the opening conduits (9i) and additive pump output control (20), simultaneously the output control valve (11) on the pipeline (9) is opened, and the input control valve (10) of the pipeline (9a) on the gasoline tank (4) opened, the homemade petrochemical industry gasoline of 90# is from additive tank (1) pipeline (9i) of flowing through, and through pipeline (9) and (9a) to export the homemade petrochemical industry gasoline of 90# to gasoline tank (4) standby for the pressure by additive pump (18) again;
Jar (1) is added in the combined additive input, cover sealing cover (17), additive pump input control valve (19) on the opening conduits (9i) and additive pump output control (20), simultaneously the output control valve (11) on the pipeline (9) is opened, and the input control valve (10) of the pipeline (9a) on the gasoline tank (4) opened, combined additive is from additive tank (1) pipeline (9i) of flowing through, and through pipeline (9) and (9a) to export combined additive to gasoline tank (4) standby for the pressure by additive pump (18) again;
Open methanol tank (2) respectively, composite additive jar (3), output control valve (11) on gasoline tank (4) and combined additive jar (5) lower channel (9b), with methyl alcohol, composite additive, gasoline and combined additive export pipeline (9c) to, again with the pressure pump (21 at pipeline (9c) two ends, 24) the pressure pump input control valve (22 on, 25) and pressure pump output control valve (23,26) open, overhead control valve (12) on the opening conduits (9d) and pipeline (9e) end connect the input control valve (10) of standby mixing tank (7) upper end simultaneously, close the input control valve (10) of mixing tank (6) upper end, methyl alcohol, composite additive, gasoline and combined additive are respectively through pipeline (9b) flow ipe (9c), by pressure pump (21,24) pressure is with methyl alcohol, composite additive, gasoline and combined additive are through pipeline (9j, 9k, 9c, 9d) and pipeline (9e) import in the standby mixing tank (7);
The circulating pressure oil pump input control valve (15a) and the circulating pressure oil pump output control valve (16a) that will connect on the pipeline (9l) of standby mixing tank (7) are opened, compounded oil flow ipe (9l) in the standby mixing tank (6), pressure by circulation pressure oil pump (14a) is in nozzle (13a) sprays into compounded oil standby mixing tank (7), carried out self-circulation 20-30 minute, the oil tank oil level of controlling standby mixing tank (7) simultaneously is at normal value, promptly become the methyl alcohol compounded oil, last opening conduits (9f) connects the output control valve (11) of standby mixing tank (7) one ends and the input control valve (10) on the pipeline (9g), close the output control valve (11) of pipeline (9f) connection mixing tank (6) one ends, the methyl alcohol compounded oil in the standby mixing tank (7) exports product tank (8) storage to through pipeline (9f) and pipeline (9g).
10. according to the preparation method of claim 7,8 or 9 described methanol composite gasolines, it is characterized in that be 30 minutes described cycling time.
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Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN102329661A (en) * | 2011-08-26 | 2012-01-25 | 陕西延长中立新能源股份有限公司 | Production process and device of methanol gasoline |
| CN102533356A (en) * | 2011-12-02 | 2012-07-04 | 刘湛 | Mixed fuel oil with energy-saving and environmental friendliness for vehicle |
| CN102827653A (en) * | 2011-06-14 | 2012-12-19 | 陈国耀 | Synthetic fuel oil with high burning rate and method for producing same |
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| CN105270771A (en) * | 2015-11-20 | 2016-01-27 | 重庆恒宇华顿新能源开发有限公司 | Distributed control linkage oil storage tank with gas concentration detection function |
| CN105446377A (en) * | 2015-11-20 | 2016-03-30 | 重庆恒宇华顿新能源开发有限公司 | Pressure increase adjustment oil storage tank for intelligently monitoring gas concentration |
| CN108587708A (en) * | 2018-02-10 | 2018-09-28 | 曹玉会 | A kind of automobile exhaust detergent and preparation method thereof |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN100516180C (en) * | 2006-03-20 | 2009-07-22 | 肖军 | High-clean methanol composite gasoline for vehicle and production thereof |
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- 2007-12-19 CN CN2007101798254A patent/CN101195771B/en not_active Expired - Fee Related
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN102002405B (en) * | 2009-09-01 | 2014-11-05 | 李国锋 | Fuel oil additive and production method thereof |
| CN102827653A (en) * | 2011-06-14 | 2012-12-19 | 陈国耀 | Synthetic fuel oil with high burning rate and method for producing same |
| CN102329661A (en) * | 2011-08-26 | 2012-01-25 | 陕西延长中立新能源股份有限公司 | Production process and device of methanol gasoline |
| CN102533356A (en) * | 2011-12-02 | 2012-07-04 | 刘湛 | Mixed fuel oil with energy-saving and environmental friendliness for vehicle |
| CN105270771A (en) * | 2015-11-20 | 2016-01-27 | 重庆恒宇华顿新能源开发有限公司 | Distributed control linkage oil storage tank with gas concentration detection function |
| CN105446377A (en) * | 2015-11-20 | 2016-03-30 | 重庆恒宇华顿新能源开发有限公司 | Pressure increase adjustment oil storage tank for intelligently monitoring gas concentration |
| CN108587708A (en) * | 2018-02-10 | 2018-09-28 | 曹玉会 | A kind of automobile exhaust detergent and preparation method thereof |
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