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 PDF

Info

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
Application number
PCT/KR2008/001932
Other languages
French (fr)
Inventor
Byong Woo Yoo
Jung Woo Yoo
Original Assignee
Vodustm Co., Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Vodustm Co., Ltd filed Critical Vodustm Co., Ltd
Publication of WO2009002008A1 publication Critical patent/WO2009002008A1/en

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/18Organic compounds containing oxygen
    • C10L1/182Organic compounds containing oxygen containing hydroxy groups; Salts thereof
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/02Liquid carbonaceous fuels essentially based on components consisting of carbon, hydrogen, and oxygen only
    • C10L1/023Liquid carbonaceous fuels essentially based on components consisting of carbon, hydrogen, and oxygen only for spark ignition
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L10/00Use of additives to fuels or fires for particular purposes
    • C10L10/10Use of additives to fuels or fires for particular purposes for improving the octane number
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L10/00Use of additives to fuels or fires for particular purposes
    • C10L10/14Use of additives to fuels or fires for particular purposes for improving low temperature properties
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L2270/00Specifically adapted fuels
    • C10L2270/02Specifically adapted fuels for internal combustion engines
    • C10L2270/023Specifically adapted fuels for internal combustion engines for gasoline engines
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L2290/00Fuel preparation or upgrading, processes or apparatus therefore, comprising specific process steps or apparatus units
    • C10L2290/24Mixing, 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.

Landscapes

  • 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
Figure imgf000005_0001
[22] Table 2 [Table 2] [Table ] Fuel composition ratio
Figure imgf000005_0002
[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
Figure imgf000007_0001
[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
Figure imgf000008_0001
[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

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.
PCT/KR2008/001932 2007-06-22 2008-04-04 The mixing alcohol fuels of high density and method of manufacture WO2009002008A1 (en)

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
WO2009002008A1 true WO2009002008A1 (en) 2008-12-31

Family

ID=40185793

Family Applications (1)

Application Number Title Priority Date Filing Date
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)

* Cited by examiner, † Cited by third party
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)

* Cited by examiner, † Cited by third party
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)

* Cited by examiner, † Cited by third party
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

Patent Citations (4)

* Cited by examiner, † Cited by third party
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)

* Cited by examiner, † Cited by third party
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

Similar Documents

Publication Publication Date Title
WO2009002008A1 (en) The mixing alcohol fuels of high density and method of manufacture
JP5129426B2 (en) Diesel fuel, its production and use
JP5674477B2 (en) Use of alcohol in fuels for spark ignition engines.
JP6782694B2 (en) Aviation fuel with renewable oxygenated material
JP5265435B2 (en) Unleaded gasoline composition for in-cylinder direct injection gasoline engine
JP3782140B2 (en) Unleaded gasoline
JP2005054102A (en) Gasoline
KR20090105931A (en) Novel single phase hydrous hydrocarbon?based fuel, methods for producing the same and compositions for use in such method
EP1167493A2 (en) Alternative fuel to gasoline
WO2014103853A1 (en) Internal combustion engine
US7314494B2 (en) Anti-detonation additive, and fuel provided therewith
WO2022235285A1 (en) Blended gasoline composition
KR100374257B1 (en) Alcoholic fuel composition
JP4429880B2 (en) Unleaded gasoline
JP4109046B2 (en) Fuel for premixed compression self-ignition engines
JP4109048B2 (en) Fuel for premixed compression self-ignition engines
JP2004285346A (en) Low pollution fuel composition
AU2017364718B2 (en) Gasoline fuel composition
JP4294519B2 (en) Gasoline composition
JP4109044B2 (en) Fuel for premixed compression self-ignition engines
JP4429881B2 (en) Unleaded high octane gasoline
JP4109052B2 (en) Fuel for premixed compression self-ignition engines
JP6448690B2 (en) Method of using fuel oil in an internal combustion engine
JP4436616B2 (en) Liquefied petroleum gas for automobiles
JP4109047B2 (en) Fuel for premixed compression self-ignition engines

Legal Events

Date Code Title Description
WWE Wipo information: entry into national phase

Ref document number: 1020087008772

Country of ref document: KR

121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 08741182

Country of ref document: EP

Kind code of ref document: A1

NENP Non-entry into the national phase

Ref country code: DE

122 Ep: pct application non-entry in european phase

Ref document number: 08741182

Country of ref document: EP

Kind code of ref document: A1