WO2009002008A1 - The mixing alcohol fuels of high density and method of manufacture - Google Patents
The mixing alcohol fuels of high density and method of manufacture Download PDFInfo
- Publication number
- WO2009002008A1 WO2009002008A1 PCT/KR2008/001932 KR2008001932W WO2009002008A1 WO 2009002008 A1 WO2009002008 A1 WO 2009002008A1 KR 2008001932 W KR2008001932 W KR 2008001932W WO 2009002008 A1 WO2009002008 A1 WO 2009002008A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- ethanol
- fuel
- methanol
- gasoline
- butanol
- Prior art date
Links
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 title claims abstract description 82
- 239000000446 fuel Substances 0.000 title claims abstract description 50
- 238000000034 method Methods 0.000 title claims description 12
- 238000002156 mixing Methods 0.000 title claims description 10
- 238000004519 manufacturing process Methods 0.000 title abstract description 5
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 claims abstract description 90
- LRHPLDYGYMQRHN-UHFFFAOYSA-N N-Butanol Chemical compound CCCCO LRHPLDYGYMQRHN-UHFFFAOYSA-N 0.000 claims abstract description 48
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 claims abstract description 48
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 claims abstract description 44
- OFBQJSOFQDEBGM-UHFFFAOYSA-N Pentane Chemical compound CCCCC OFBQJSOFQDEBGM-UHFFFAOYSA-N 0.000 claims abstract description 20
- 239000000463 material Substances 0.000 claims abstract description 13
- 125000003118 aryl group Chemical group 0.000 claims abstract description 12
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 claims abstract description 10
- 239000008096 xylene Substances 0.000 claims abstract description 10
- UFWIBTONFRDIAS-UHFFFAOYSA-N Naphthalene Chemical compound C1=CC=CC2=CC=CC=C21 UFWIBTONFRDIAS-UHFFFAOYSA-N 0.000 claims description 2
- 239000003502 gasoline Substances 0.000 abstract description 31
- 238000002485 combustion reaction Methods 0.000 abstract description 7
- 230000000694 effects Effects 0.000 abstract description 4
- 230000008014 freezing Effects 0.000 abstract description 4
- 238000007710 freezing Methods 0.000 abstract description 4
- 238000003912 environmental pollution Methods 0.000 abstract description 2
- 230000002265 prevention Effects 0.000 abstract description 2
- 239000003981 vehicle Substances 0.000 description 7
- 239000002360 explosive Substances 0.000 description 5
- 239000000203 mixture Substances 0.000 description 5
- 239000004094 surface-active agent Substances 0.000 description 5
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 3
- 230000003247 decreasing effect Effects 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 239000003921 oil Substances 0.000 description 2
- 238000011056 performance test Methods 0.000 description 2
- 230000002035 prolonged effect Effects 0.000 description 2
- 239000004071 soot Substances 0.000 description 2
- 238000003860 storage Methods 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 1
- 239000005977 Ethylene Substances 0.000 description 1
- 238000013019 agitation Methods 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- -1 low output power Chemical compound 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000010705 motor oil Substances 0.000 description 1
- TVMXDCGIABBOFY-UHFFFAOYSA-N octane Chemical compound CCCCCCCC TVMXDCGIABBOFY-UHFFFAOYSA-N 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000000779 smoke Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
Classifications
-
- 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
-
- 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
- C10L1/023—Liquid carbonaceous fuels essentially based on components consisting of carbon, hydrogen, and oxygen only for spark ignition
-
- 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
- C10L10/10—Use of additives to fuels or fires for particular purposes for improving the octane number
-
- 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
-
- 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
-
- 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
- C10L2290/00—Fuel preparation or upgrading, processes or apparatus therefore, comprising specific process steps or apparatus units
- C10L2290/24—Mixing, stirring of fuel components
Definitions
- the present invention relates to a high density mixed alcohol fuel, which is prepared by using methanol or ethanol as a main material. More particularly, the present invention relates to a high density mixed alcohol fuel, in which 35 to 45 wt% of methanol or ethanol, 5 to 7wt% of isopropanol, 5 to 8 wt% of butanol, 15 to 25wt% of toluene, 5 to 10 wt% of non-aromatic raffinate, 5 to 10 wt% of pentane, 15 to 25wt% of naphtha, and 5 to 10 wt% of xylene are sequentially mixed, or in which 10 to 25 wt% of methanol or ethanol, 4 to 14 wt% of C5, 4 to 14 wt% of mixed oil, 50 to 55wt% of naphtha, 1 to 6wt% of isopropanol, 10 to 15wt% of MTB, 5 to 9wt% of aromatics, and
- methanol or ethanol itself has a low freezing point, a high specific gravity, a wide combustion range, and a low calorific value.
- methanol or ethanol has a disadvantage in that output power is not high. Accordingly, the most fundamental problem in applying methanol to a gasoline vehicle is to reduce the upper flash point of an explosive mixture air to a level of gasoline.
- an octane number is increased up to 125 or more, and the emission amount of exhaust gas (which is one of the main worldwide pollution issues) is largely reduced, thereby increasing output power.
- the present invention it is possible to solve the problem of low start ability at low temperatures, which is one defect of ethanol. Since butanol is added, the low temperature start ability may be improved, and the freezing point of a fuel may be reduced compared to gasoline so that usability can be higher than gasoline, even in a cold environment. In addition, in a tropical region, the fuel can be used only by changing butanol alcohol to methanol or ethanol and mixing the material in an appropriate ratio.
- the present invention relates to a high density mixed alcohol fuel, in which methanol or ethanol as a main material is mixed in a predetermined ratio, thereby generating I.P.A (isopropanol) functioning as a surfactant. Accordingly, the contents of butanol (alcohol) having low temperature start ability, toluene, and modified gasoline are increased, thereby improving explosive power.
- the present invention provides a high density mixed alcohol fuel including methanol or ethanol as a main material, in which I.P.A (isopropanol) functioning as a surfactant is generated, thereby increasing thecontent of butanol (alcohol) having low temperature start ability, separating toluene capable of improving explosive power, and achieving -18 0 C to -2O 0 C of the upper flash point.
- I.P.A isopropanol
- butanol alcohol
- the fuel according to the present invention may include 35 to 45 wt% of methanol or ethanol, 5 to 7wt% of isopropanol, 5 to 8 wt% of butanol, 15 to 25wt% of toluene, 5 to 10 wt% of non-aromatic raffinate, 5 to 10 wt% of pentane, 15 to 25wt% of naphtha, and 5 to 10 wt% of xylene.
- the fuel according to the present invention may include 10 to 25 wt% of methanol or ethanol, 4 to 14 wt% of pentane, 4 to 14 wt% of mixed oil, 50 to 55wt% of naphtha, 1 to 6wt% of isopropanol, 10 to 15wt% of MTB, 5 to 9wt% of aromatics, and 1 to 7wt% of butanol.
- the present invention provides a method of sequentially mixing a) 35 to
- the present invention provides a method of sequentially mixing a) 10 to 50 to 55wt% of naphtha: e) 1 to 6wt% of isopropanol: f) 10 to 15wt% of MTB: g) 5 to 9wt% of aromatics: and h) 1 to 7wt% of butanol.
- the present invention provides a high density mixed alcohol fuel by sequentially mixing the above enumerated materials.
- isopropanol operates as a surfactant
- butanol allows an engine to be easily started at low temperatures, and toluene improves explosive power.
- non-aromatic raffinate is added, instead of reformed gasoline, in a mixed fuel of Korea Patent No. 0242667, so as to inhibit vapor condensation caused by the reformed gasoline and to improve explosive power and ignitibility.
- non-aromatic raffinate is usually generated as a by-product in the process of extracting aromatic chemicals (benzene, toluene, and xylene) from cracked gasoline (RPG), the cracked gasoline being obtained during a process of obtaining ethylene by naphtha cracking, and can be used as a solvent.
- aromatic chemicals benzene, toluene, and xylene
- the fuel according to the present invention can replace conventional gasoline due to a reduced production cost, and can reduce the amount of exhaust gas due to complete combustion of ethanol, thereby achieving an environmental pollution prevention effect. Also, the fuel can be directly applied to a vehicle without changing an inlet device or an inlet port of the vehicle. Also, since the fuel has almost the same output power as gasoline, and a freezing point lower than gasoline, it is possible to maintain start ability of the vehicle, even in a cold environment. Mode for the Invention
- Example 1 Preparation of a mixed alcohol fuel
- Fuels having composition ratios according to Table 1 and Table 2 were prepared. In preparing fuels, respective materials were sequentially mixed at room temperature and at atmospheric pressure, and were subjected to agitation so that mixing could be entirely sufficiently carried out.
- Example 2 Comparison between gasoline and a mixed fuel [25] According to the following ratio and order, methanol, I.P.A (isopropanol) functioning as a surfactant, butanol (alcohol), and toluene were mixed.
- the mixing was carried at the same temperature and at atmospheric pressure, and in order to entirely uniformly mix the materials, an appropriate mixer was introduced.
- the modified gasoline indicates non-aromatic raffinate, pentane, naphtha, and xylene.
- the mixed fuel according to the present invention has almost the same fuel efficiency as gasoline. Accordingly, in consideration of the lower production cost of the mixed fuel than gasoline, it is possible to achieve a cost reduction effect. Also, the complete combustion of alcohol materials and other various mixed materials widens the range of combustion, and thus increases the output power, thereby decreasing the amount of exhaust gas by 50% with respect to a gasoline-powered vehicle.
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- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Liquid Carbonaceous Fuels (AREA)
- Health & Medical Sciences (AREA)
- Emergency Medicine (AREA)
Abstract
Disclosed is a high density mixed alcohol fuel, which is prepared by using methanol or ethanol as a main material. More particularly, in the disclosed high density mixed alcohol fuel, 35 to 45 wt% of methanol or ethanol, 5 to 7wt% of isopropanol, 5 to 8 wt% of butanol, 15 to 25wt% of toluene, 5 to 10 wt% of non-aromatic raffinate, 5 to 10 wt% of pentane, 15 to 25wt% of naphtha, and 5 to 10 wt% of xylene are sequentially mixed; or 10 to 25 wt% of methanol or ethanol, 4 to 14 wt% of C5, 4 to 14 wt% of mixed oil, 50 to 55wt% of naphtha, 1 to 6wt% of isopropanol, 10 to 15wt% of MTB, 5 to 9wt% of aromatics, and 1 to 7wt% of butanol are sequentially mixed. Accordingly, the fuel can replace conventional gasoline due to a reduced production cost, and can reduce the amount of exhaust gas due to complete combustion of ethanol, thereby achieving an environmental pollution prevention effect. Also, it is possible to directly apply the fuel to a vehicle without changing an inlet device or an inlet port of the vehicle. Also, since the fuel has almost the same output power as gasoline, and a freezing point lower than gasoline, it is possible to maintain start ability of the vehicle, even in a cold environment.
Description
Description
THE MIXING ALCOHOL FUELS OF HIGH DENSITY AND METHOD OF MANUFACTURE
Technical Field
[1] The present invention relates to a high density mixed alcohol fuel, which is prepared by using methanol or ethanol as a main material. More particularly, the present invention relates to a high density mixed alcohol fuel, in which 35 to 45 wt% of methanol or ethanol, 5 to 7wt% of isopropanol, 5 to 8 wt% of butanol, 15 to 25wt% of toluene, 5 to 10 wt% of non-aromatic raffinate, 5 to 10 wt% of pentane, 15 to 25wt% of naphtha, and 5 to 10 wt% of xylene are sequentially mixed, or in which 10 to 25 wt% of methanol or ethanol, 4 to 14 wt% of C5, 4 to 14 wt% of mixed oil, 50 to 55wt% of naphtha, 1 to 6wt% of isopropanol, 10 to 15wt% of MTB, 5 to 9wt% of aromatics, and 1 to 7wt% of butanol are sequentially mixed. Background Art
[2] Compared to gasoline, methanol or ethanol itself has a low freezing point, a high specific gravity, a wide combustion range, and a low calorific value. Thus, when used as a fuel for a vehicle, methanol or ethanol has a disadvantage in that output power is not high. Accordingly, the most fundamental problem in applying methanol to a gasoline vehicle is to reduce the upper flash point of an explosive mixture air to a level of gasoline.
[3] In the present invention, in order to solve the above described problem, butanol and toluene are mixed in a certain ratio. Thus, the upper flash point is reduced to -180C to - 2O0C so that stability can be secured, and vapor pressure is adjusted to 0.705kg/cm.
[4] Also, in the present invention, an octane number is increased up to 125 or more, and the emission amount of exhaust gas (which is one of the main worldwide pollution issues) is largely reduced, thereby increasing output power.
[5] Also, in the present invention, since toluene is added, several problems caused by an insufficient calorific value of methanol, such as low output power, low fuel efficiency, and economical inefficiency, may be solved. In addition, a mixed fuel can be completely combusted, and fuel efficiency and economical efficiency may be increased. Also, the complete combustion can largely reduce the emission amount of exhaust gas.
[6] Also, in the present invention, it is possible to solve the problem of low start ability at low temperatures, which is one defect of ethanol. Since butanol is added, the low temperature start ability may be improved, and the freezing point of a fuel may be reduced compared to gasoline so that usability can be higher than gasoline, even in a
cold environment. In addition, in a tropical region, the fuel can be used only by changing butanol alcohol to methanol or ethanol and mixing the material in an appropriate ratio.
[7] Also, in order to inhibit separation of a non-aqueous solution and to maintain the stability during prolonged storage, methanol (aqueous) is added, and thus I.P.A (isopropanol) functioning as a surfactant is generated. Accordingly, it is possible to prevent deterioration during storage, reinforce stability, and store the fuel in the same manner as gasoline.
[8] Therefore, in the present invention, methanol or ethanol is mixed with the following chemical materials in a predetermined ratio to achieve a better fuel than gasoline. Disclosure of Invention Technical Problem
[9] Therefore, the present invention relates to a high density mixed alcohol fuel, in which methanol or ethanol as a main material is mixed in a predetermined ratio, thereby generating I.P.A (isopropanol) functioning as a surfactant. Accordingly, the contents of butanol (alcohol) having low temperature start ability, toluene, and modified gasoline are increased, thereby improving explosive power. Technical Solution
[10] The present invention provides a high density mixed alcohol fuel including methanol or ethanol as a main material, in which I.P.A (isopropanol) functioning as a surfactant is generated, thereby increasing thecontent of butanol (alcohol) having low temperature start ability, separating toluene capable of improving explosive power, and achieving -180C to -2O0C of the upper flash point.
[11] Preferably, the fuel according to the present invention may include 35 to 45 wt% of methanol or ethanol, 5 to 7wt% of isopropanol, 5 to 8 wt% of butanol, 15 to 25wt% of toluene, 5 to 10 wt% of non-aromatic raffinate, 5 to 10 wt% of pentane, 15 to 25wt% of naphtha, and 5 to 10 wt% of xylene.
[12] Preferably, the fuel according to the present invention may include 10 to 25 wt% of methanol or ethanol, 4 to 14 wt% of pentane, 4 to 14 wt% of mixed oil, 50 to 55wt% of naphtha, 1 to 6wt% of isopropanol, 10 to 15wt% of MTB, 5 to 9wt% of aromatics, and 1 to 7wt% of butanol.
[13] Preferably, the present invention provides a method of sequentially mixing a) 35 to
45 wt% of methanol or ethanol: b) 5 to 7wt% of isopropanol: c) 5 to 8 wt% of butanol: d) 15 to 25wt% of toluene: e) 5 to 10 wt% of non-aromatic raffinate: f) 5 to 10 wt% of pentane: g) 15 to 25wt% of naphtha: and h) 5 to 10 wt% of xylene.
[14] Preferably, the present invention provides a method of sequentially mixing a) 10 to
50 to 55wt% of naphtha: e) 1 to 6wt% of isopropanol: f) 10 to 15wt% of MTB: g) 5 to 9wt% of aromatics: and h) 1 to 7wt% of butanol.
[15] Preferably, the present invention provides a high density mixed alcohol fuel by sequentially mixing the above enumerated materials.
[16] Preferably, isopropanol operates as a surfactant, butanol allows an engine to be easily started at low temperatures, and toluene improves explosive power. Also, non-aromatic raffinate is added, instead of reformed gasoline, in a mixed fuel of Korea Patent No. 0242667, so as to inhibit vapor condensation caused by the reformed gasoline and to improve explosive power and ignitibility. In addition, the non-aromatic raffinate is usually generated as a by-product in the process of extracting aromatic chemicals (benzene, toluene, and xylene) from cracked gasoline (RPG), the cracked gasoline being obtained during a process of obtaining ethylene by naphtha cracking, and can be used as a solvent.
Advantageous Effects
[17] The fuel according to the present invention can replace conventional gasoline due to a reduced production cost, and can reduce the amount of exhaust gas due to complete combustion of ethanol, thereby achieving an environmental pollution prevention effect. Also, the fuel can be directly applied to a vehicle without changing an inlet device or an inlet port of the vehicle. Also, since the fuel has almost the same output power as gasoline, and a freezing point lower than gasoline, it is possible to maintain start ability of the vehicle, even in a cold environment. Mode for the Invention
[18] Example
[19] Example 1: Preparation of a mixed alcohol fuel
[20] Fuels having composition ratios according to Table 1 and Table 2 were prepared. In preparing fuels, respective materials were sequentially mixed at room temperature and at atmospheric pressure, and were subjected to agitation so that mixing could be entirely sufficiently carried out.
[21] Table 1
[Table 1]
[Table ]
Fuel composition ratio
[22] Table 2 [Table 2] [Table ] Fuel composition ratio
[23] [24] Example 2: Comparison between gasoline and a mixed fuel [25] According to the following ratio and order, methanol, I.P.A (isopropanol) functioning as a surfactant, butanol (alcohol), and toluene were mixed.
[26] Methanol (or ethanol) 35 wt% [27] isopropanol 15 wt% [28] butanol 5 wt%
[29] toluene 25 wt%
[30] modified gasoline 20 wt%
[31] In an appropriate vessel (tube), the mixing was carried at the same temperature and at atmospheric pressure, and in order to entirely uniformly mix the materials, an appropriate mixer was introduced. Herein, the modified gasoline indicates non-aromatic raffinate, pentane, naphtha, and xylene.
[32] Table 3
[Table 3]
[Table ]
Comparison table of fuel state
[33] As noted in Table 3, in the mixed fuel prepared according to the present invention, a specific gravity was about 0.805 to 0.815 (which is similar to gasoline of 0.7 to 0.8), a flash point was -180C to -2O0C (which is uniformly stable), and an ignition point was also on a level with gasoline. Also, vapor pressure was 0.705, which is within a range
of 0.45 to 0.80 (a gasoline basis value) and was relatively stably maintained. [34] In addition, in a corrosion test on a copper plate, the mixed fuel according to the present invention proved to be better due to lower corrosiveness than conventional gasoline, and also, in a smoke soot test, the produced amount of soot of the mixed fuel was less than conventional gasoline. [35] Example 3: Test on vehicles
[36] Table 4
[Table 4]
[Table ] test results on vehicles
[37] As noted in Table 4, the mixed fuel according to the present invention has almost the same fuel efficiency as gasoline. Accordingly, in consideration of the lower production cost of the mixed fuel than gasoline, it is possible to achieve a cost reduction effect. Also, the complete combustion of alcohol materials and other various mixed materials widens the range of combustion, and thus increases the output power, thereby decreasing the amount of exhaust gas by 50% with respect to a gasoline-powered vehicle.
[38] In addition, the performance test using a clarifier for preparing gasoline was carried out in the same manner of the gasoline performance test, and thus it was determined that motor performance was desirably maintained at -2O0C. Also, compared to gasoline, it was determined that the mixed fuel had better combustion conditions, did not impose a burden on a motor by reducing the motor s own calorific value, did not generate carbons, prolonged the life of the motor and motor oil, and significantly decreased vibrations and noise. Industrial Applicability
[39] While this invention has been described in connection with what is presently considered to be the most practical and preferred embodiment, it is to be understood that the invention is not limited to the disclosed embodiment and the drawings. On the contrary, it is intended to cover various modifications and variations within the spirit and scope of the appended claims.
Claims
[1] A high density mixed alcohol fuel comprised of methanol or ethanol as a main material, the fuel comprising methanol or ethanol, isopropanol, butanol, toluene, non-aromatic raffinate, pentane, naphtha, and xylene.
[2] A high density mixed alcohol fuel comprised of methanol or ethanol as a main material, the fuel comprising methanol or ethanol, C5, mixed oil, naphtha, isopropanol, MTB, aromatics, and, butanol.
[3] The high density mixed alcohol fuel as claimed in claim 1, which is comprised of
35 to 45 wt% of methanol or ethanol, 5 to 7wt% of isopropanol, 5 to 8 wt% of butanol, 15 to 25wt% of toluene, 5 to 10 wt% of non-aromatic raffinate, 5 to 10 wt% of pentane, 15 to 25wt% of naphtha, and 5 to 10 wt% of xylene.
[4] The high density mixed alcohol fuel as claimed in claim 2, which is comprised of
10 to 25 wt% of methanol or ethanol, 4 to 14 wt% of C5, 4 to 14 wt% of mixed oil, 50 to 55wt% of naphtha, 1 to 6wt% of isopropanol, 10 to 15wt% of MTB, 5 to 9wt% of aromatics, and 1 to 7wt% of butanol.
[5] A method of preparing a high density mixed alcohol fuel, the method comprising the step of; mixing sequentially a) methanol or ethanol: b) isopropanol: c) butanol: d) toluene: e) non-aromatic raffinate: f) pentane: g) naphtha: and h) xylene.
[6] The method as claimed in claim 5, wherein the high density mixed alcohol fuel is comprised of 35 to 45 wt% of methanol or ethanol, 5 to 7wt% of isopropanol, 5 to 8 wt% of butanol, 15 to 25wt% of toluene, 5 to 10 wt% of non-aromatic raffinate, 5 to 10 wt% of pentane, 15 to 25wt% of naphtha, and 5 to 10 wt% of xylene.
[7] A method of preparing a high density mixed alcohol fuel, the method comprising the step of; mixing sequentially a) methanol or ethanol: b) C5: c) mixed oil: d) naphtha: e) isopropanol: f) MTB: g) aromatics: and h) butanol.
[8] The method as claimed in claim 7, wherein the high density mixed alcohol fuel is comprised of 10 to 25 wt% of methanol or ethanol, 4 to 14 wt% of C5, 4 to 14 wt% of mixed oil, 50 to 55wt% of naphtha, 1 to 6wt% of isopropanol, 10 to 15wt% of MTB, 5 to 9wt% of aromatics, and 1 to 7wt% of butanol.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN200710123333.3 | 2007-06-22 | ||
CNA2007101233333A CN101328438A (en) | 2007-06-22 | 2007-06-22 | High concentration mixing alcohol fuel and preparation thereof |
Publications (1)
Publication Number | Publication Date |
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WO2009002008A1 true WO2009002008A1 (en) | 2008-12-31 |
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Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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PCT/KR2008/001932 WO2009002008A1 (en) | 2007-06-22 | 2008-04-04 | The mixing alcohol fuels of high density and method of manufacture |
Country Status (3)
Country | Link |
---|---|
KR (1) | KR20090003146A (en) |
CN (1) | CN101328438A (en) |
WO (1) | WO2009002008A1 (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103937562A (en) * | 2014-05-04 | 2014-07-23 | 黔东南道燃新能源有限公司 | Clean fuel and preparation method thereof |
CN105154145A (en) * | 2015-07-14 | 2015-12-16 | 贵州天鼎新能源有限公司 | M100 methanol fuel |
CN106336887A (en) * | 2015-07-09 | 2017-01-18 | 岳阳市中发科技有限公司 | Production method for hydrocarbon oil |
RU2641108C1 (en) * | 2016-12-23 | 2018-01-16 | Акционерное общество "Всероссийский научно-исследовательский институт по переработке нефти" (АО "ВНИИ НП") | Alternative motor fuel |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR102012771B1 (en) * | 2016-11-10 | 2019-08-21 | 주식회사 삼형에너지 | Fuel composition containing methanol for internal combustion engine |
CN107513440A (en) * | 2017-09-21 | 2017-12-26 | 王高华 | Alcohol fuel and preparation method and application |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5242469A (en) * | 1990-06-07 | 1993-09-07 | Tonen Corporation | Gasoline additive composition |
US5498809A (en) * | 1992-12-17 | 1996-03-12 | Exxon Chemical Patents Inc. | Polymers derived from ethylene and 1-butene for use in the preparation of lubricant dispersant additives |
US5698722A (en) * | 1992-12-17 | 1997-12-16 | Exxon Chemical Patents Inc. | Functionalization of polymers based on Koch chemistry and derivatives thereof |
US5814715A (en) * | 1992-12-17 | 1998-09-29 | Exxon Chemical Patents Inc | Amorphous olefin polymers, copolymers, methods of preparation and derivatives thereof |
-
2007
- 2007-06-22 CN CNA2007101233333A patent/CN101328438A/en active Pending
-
2008
- 2008-04-04 WO PCT/KR2008/001932 patent/WO2009002008A1/en active Application Filing
- 2008-04-04 KR KR1020087008772A patent/KR20090003146A/en not_active Application Discontinuation
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5242469A (en) * | 1990-06-07 | 1993-09-07 | Tonen Corporation | Gasoline additive composition |
US5498809A (en) * | 1992-12-17 | 1996-03-12 | Exxon Chemical Patents Inc. | Polymers derived from ethylene and 1-butene for use in the preparation of lubricant dispersant additives |
US5698722A (en) * | 1992-12-17 | 1997-12-16 | Exxon Chemical Patents Inc. | Functionalization of polymers based on Koch chemistry and derivatives thereof |
US5814715A (en) * | 1992-12-17 | 1998-09-29 | Exxon Chemical Patents Inc | Amorphous olefin polymers, copolymers, methods of preparation and derivatives thereof |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103937562A (en) * | 2014-05-04 | 2014-07-23 | 黔东南道燃新能源有限公司 | Clean fuel and preparation method thereof |
CN103937562B (en) * | 2014-05-04 | 2016-02-03 | 贵阳白云合协生产力促进中心有限责任公司 | Clean fuel and preparation method thereof |
CN106336887A (en) * | 2015-07-09 | 2017-01-18 | 岳阳市中发科技有限公司 | Production method for hydrocarbon oil |
CN105154145A (en) * | 2015-07-14 | 2015-12-16 | 贵州天鼎新能源有限公司 | M100 methanol fuel |
RU2641108C1 (en) * | 2016-12-23 | 2018-01-16 | Акционерное общество "Всероссийский научно-исследовательский институт по переработке нефти" (АО "ВНИИ НП") | Alternative motor fuel |
Also Published As
Publication number | Publication date |
---|---|
KR20090003146A (en) | 2009-01-09 |
CN101328438A (en) | 2008-12-24 |
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