CN103937561A - Composite biomass liquid fuel - Google Patents
Composite biomass liquid fuel Download PDFInfo
- Publication number
- CN103937561A CN103937561A CN201410144326.1A CN201410144326A CN103937561A CN 103937561 A CN103937561 A CN 103937561A CN 201410144326 A CN201410144326 A CN 201410144326A CN 103937561 A CN103937561 A CN 103937561A
- Authority
- CN
- China
- Prior art keywords
- additive
- liquid fuel
- raw material
- methanol
- main raw
- Prior art date
- Legal status (The legal status 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 status listed.)
- Pending
Links
Landscapes
- Liquid Carbonaceous Fuels (AREA)
Abstract
The invention relates to a composite biomass liquid fuel which is prepared by adding 5-8wt% of additive and compounding through taking fine methanol (the purity of which is 99.9%) as a main active ingredient; the additive comprises the following main active ingredients: methanol, n-butanol, potassium permanganate, methylbenzene, tung oil, camphorated oil, acetone, hydrogen peroxide and ferrocene. The composite biomass liquid fuel has the advantages of being stored, used and transported under no pressure at normal temperature, being strong in hydrophilicity, capable of being put out with once watering, free from no residues, capable of normal burning at minus 35DEG C, free from CO emission, with the calorific value of 8500-9000 kilocaloride and flame temperature of 1000-1150DEG C, and capable of lowering the cost by 20-25% compared with liquefied gas.
Description
technical field:
The present invention relates to a kind of compound raw matter liquid fuel.
Background technology
The energy is the basis of developing national economy, it is again the necessary resource that people depend on for existence, development along with scientific-technical progress and human civilization, the demand of civil liquid fuel is increasing, and along with the enhancing of environmental consciousness, people are also more and more higher to the requirement of fuel, and the mineral fuel supply day that the oil of take is representative is becoming tight, and price also occupy high-leveled and difficult under; Petroleum resources shortage is global, and the petroleum resources of China are not abundant, and the demand in considerable city to domestic fuel, biases toward diesel oil, liquefied gas, natural gas, piped gas equal energy source day by day; Existing most of hotels, restaurant are used diesel oil as fuel, during burning, because burning is insufficient, have cigarette, have taste, and the concentration of the carbon monoxide of discharge is higher, easily causes environmental pollution; Sweet natural gas and coal gas are not all installed by most resident family, coal or the oil liquefied gas of adopting are done the energy more, coal or oil liquefied gas produce harmful flue gas in combustion processes, contaminate environment, cost is high, changes tank inconvenience, makes these non-renewable energy growing tensions, so people, in the urgent need to energy regenerated fuel, can only replace present fuel with bioenergy.
Summary of the invention
In order to overcome above-mentioned defect, the object of this invention is to provide a kind of safe, inexpensive, without the compound raw matter liquid fuel of noxious gas emission, free from extraneous odour.
To achieve these goals, the present invention adopts following technical scheme:
A compound raw matter liquid fuel, it is that to take refined methanol (liquid methanol of purity 99.9%) be main raw material, adds the additive of 5-8%, is composited; Additive main raw material: methyl alcohol, propyl carbinol, too quickly sour potassium, toluene, tung oil, white oil of camphor, acetone, hydrogen peroxide, ferrocene.
Take refined methanol as main raw material, the additive that adds 5-8%, additive main raw material weight proportion is: the too quickly sour potassium of methyl alcohol (5-10%) propyl carbinol (40-50%) (30-40%) toluene (0.1-0.2%) tung oil (10-20%) white oil of camphor (0.1-0.2%) acetone (0.1-0.2%) hydrogen peroxide (0.1-0.2%) ferrocene (0.1-0.2%).
Advantage of the present invention: without storage under pressure normal temperature, use, transportation, wetting ability is strong, water and go out, without residue ,-35 degree trouble-free burning, without CO discharge, calorific value 8500-9000 kilocalorie, flame temperature 1000-1150 degree, cost than the low 20-25% of liquefied gas.
Embodiment
Below by embodiment, further illustrate:
Embodiment 1, a kind of compound raw matter liquid fuel, and it is to take refined methanol as main raw material, adds the additive of 5-8%, is composited; Additive main raw material: the too quickly sour potassium toluene tung oil white oil of camphor acetone hydrogen peroxide ferrocene of methyl alcohol propyl carbinol.Refined methanol is the liquid methanol of 99.9% purity.
Take refined methanol as main raw material, the additive that adds 5-8%, additive main raw material weight proportion is: the too quickly sour potassium of methyl alcohol (9%) propyl carbinol (40%) (30%) toluene (0.2%) tung oil (20%) white oil of camphor (0.2%) acetone (0.2%) hydrogen peroxide (0.2%) ferrocene (0.2%).
Embodiment 2, a kind of compound raw matter liquid fuel, and it is to take refined methanol as main raw material, adds the additive of 5-8%, is composited; Additive main raw material: the too quickly sour potassium toluene tung oil white oil of camphor acetone hydrogen peroxide ferrocene of methyl alcohol propyl carbinol.Refined methanol is the liquid methanol of 99.9% purity.
Take refined methanol as main raw material, the additive that adds 5-8%, additive main raw material weight proportion is: the too quickly sour potassium of methyl alcohol (7.5%) propyl carbinol (50%) (30%) toluene (0.1%) tung oil (12%) white oil of camphor (0.1%) acetone (0.1%) hydrogen peroxide (0.1%) ferrocene (0.1%).
Claims (2)
1. a compound raw matter liquid fuel, it is that to take refined methanol (liquid methanol of purity 99.9%) be main raw material, adding weight proportion is the additive of 5-8%, be composited, additive main raw material: methyl alcohol, propyl carbinol, too quickly sour potassium, toluene, tung oil, white oil of camphor, acetone, hydrogen peroxide, ferrocene.
2. compound raw matter liquid fuel according to claim 1, it is characterized in that: take refined methanol as main raw material, the additive that adds 5-8%, additive main raw material weight proportion is: the too quickly sour potassium of methyl alcohol (5-10%) propyl carbinol (40-50%) (30-40%) toluene (0.1-0.2%) tung oil (10-20%) white oil of camphor (0.1-0.2%) acetone (0.1-0.2%) hydrogen peroxide (0.1-0.2%) ferrocene (0.1-0.2%).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201410144326.1A CN103937561A (en) | 2014-04-11 | 2014-04-11 | Composite biomass liquid fuel |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201410144326.1A CN103937561A (en) | 2014-04-11 | 2014-04-11 | Composite biomass liquid fuel |
Publications (1)
Publication Number | Publication Date |
---|---|
CN103937561A true CN103937561A (en) | 2014-07-23 |
Family
ID=51185442
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201410144326.1A Pending CN103937561A (en) | 2014-04-11 | 2014-04-11 | Composite biomass liquid fuel |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN103937561A (en) |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1458246A (en) * | 2002-05-15 | 2003-11-26 | 吉恒 | Liquid fuel and its preparing method |
CN1928032A (en) * | 2006-04-04 | 2007-03-14 | 高顺泉 | Environmental protection energy-saving liquid fuel for cooking stove |
CN101921630A (en) * | 2009-06-17 | 2010-12-22 | 李德军 | Novel bio-alcohol oil fuel |
CN101955819A (en) * | 2009-07-17 | 2011-01-26 | 东莞市智造生物科技有限公司 | Biomass nano-fuel combustion-support additive |
JP2011207920A (en) * | 2010-03-29 | 2011-10-20 | Jfe Techno Research Corp | Method and apparatus for producing fuel oil from biomass material |
-
2014
- 2014-04-11 CN CN201410144326.1A patent/CN103937561A/en active Pending
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1458246A (en) * | 2002-05-15 | 2003-11-26 | 吉恒 | Liquid fuel and its preparing method |
CN1928032A (en) * | 2006-04-04 | 2007-03-14 | 高顺泉 | Environmental protection energy-saving liquid fuel for cooking stove |
CN101921630A (en) * | 2009-06-17 | 2010-12-22 | 李德军 | Novel bio-alcohol oil fuel |
CN101955819A (en) * | 2009-07-17 | 2011-01-26 | 东莞市智造生物科技有限公司 | Biomass nano-fuel combustion-support additive |
JP2011207920A (en) * | 2010-03-29 | 2011-10-20 | Jfe Techno Research Corp | Method and apparatus for producing fuel oil from biomass material |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
MX2018002109A (en) | Fuels and fuel additives that have high biogenic content derived from renewable organic feedstock. | |
CO6710920A2 (en) | Methods to improve bio-oil for hydrocarbon fuels, intended for transport | |
Bondarenko et al. | An overview and prospectives of practical application of the biomass gasification technology in Ukraine | |
Shah et al. | Perspectives of biogas conversion into Bio-CNG for automobile fuel in Bangladesh | |
AR072674A1 (en) | A METHOD FOR THE PRODUCTION OF LIGHT HYDROCARBONS FROM GAS WITH HIGH CONTENT OF METHANE, A SOLID OXIDE FUEL CELL USED FOR THE PRODUCTION OF LIGHT HYDROCARBONS FROM GAS WITH HIGH CONTENT OF METHANE AND A LIQUID HYDROID PRODUCTION CATALYZER | |
EA201490089A1 (en) | METHOD OF REGULATING THE RELATION OF HYDROGEN TO CARBON MONOXIDE IN SYNTHESIS GAS | |
BR112016002207A2 (en) | thermochemical conversion method of a carbonic charge to a synthesis gas containing mainly hydrogen (h2) and carbon monoxide (co) | |
Broderick et al. | Has US Shale Gas Reduced CO2 emissions? Examining recent changes in emissions from the US power sector and traded fossil fuels: Examining recent changes in emissions from the US power sector and traded fossil fuels | |
GB0812618D0 (en) | The economic conversion of waste carbon dioxide gas such as that produced by fossil fuel burning power stations, to bulk liquid fuels suitable for automabiles | |
CO6440517A2 (en) | PROCESS WITHOUT FRACTIONATION FOR THE PRODUCTION OF LOW-POINT FUEL OIL FUEL PRODUCTION OR FRACTIONS OF THE SAME | |
CN103937561A (en) | Composite biomass liquid fuel | |
Broderick et al. | Has US shale gas reduced CO2 emissions? Examining recent changes in emissions from the US power sector and traded fossil fuels | |
CN103897749B (en) | Alcohol-group fuel that a kind of complete thermo-efficiency that burns is high and preparation method thereof | |
WO2012082398A3 (en) | Fuel compositions and methods based on biomass pyrolysis | |
JP7075062B2 (en) | Carbon fiber that can be reproducibly or partially reproducibly produced from CO2 using a combined production method | |
Kijeński | Biorefineries-from biofuels to the chemicalization of agricultural products | |
CN203373145U (en) | Immersed gas production device of pentane oil | |
CN102965159A (en) | Synthetic gasoline | |
CN103602352B (en) | A kind of Low-carbon efficient alcohol oil and preparation method thereof | |
Bhattacharya | Sustained growth of green energy economics | |
Ramadhas | Fuels and trends | |
Izah et al. | Bioenergy Potential of under-utilized solid waste residues from oil palm mills in Nigeria | |
Ingawale et al. | Comparative study of a performance of an internal combustion engine and its emission working on conventional fuel (Diesel) and alternative fuel (Bio-CNG) | |
Percy et al. | A comprehensive review on the production and enhancement techniques of gaseous biofuels and their applications in IC engines with special reference to the associated performance and emission characteristics | |
CN104371765A (en) | Liquid fuel |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
AD01 | Patent right deemed abandoned |
Effective date of abandoning: 20161116 |
|
C20 | Patent right or utility model deemed to be abandoned or is abandoned |