CN107723036A - The alcohol-based fuel of not smoked eye during use - Google Patents
The alcohol-based fuel of not smoked eye during use Download PDFInfo
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- 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
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- C10L1/00—Liquid carbonaceous fuels
- C10L1/10—Liquid carbonaceous fuels containing additives
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- 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
- C10L10/04—Use of additives to fuels or fires for particular purposes for minimising corrosion or incrustation
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- 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
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- 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
- C10L10/12—Use of additives to fuels or fires for particular purposes for improving the cetane number
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- 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
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- 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
- C10L1/12—Inorganic compounds
- C10L1/1225—Inorganic compounds halogen containing compounds
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- 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
- C10L1/16—Hydrocarbons
- C10L1/1616—Hydrocarbons fractions, e.g. lubricants, solvents, naphta, bitumen, tars, terpentine
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- 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
- C10L1/16—Hydrocarbons
- C10L1/1691—Hydrocarbons petroleum waxes, mineral waxes; paraffines; alkylation products; Friedel-Crafts condensation products; petroleum resins; modified waxes (oxidised)
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- 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
- C10L1/1822—Organic compounds containing oxygen containing hydroxy groups; Salts thereof hydroxy group directly attached to (cyclo)aliphatic carbon atoms
- C10L1/1824—Organic compounds containing oxygen containing hydroxy groups; Salts thereof hydroxy group directly attached to (cyclo)aliphatic carbon atoms mono-hydroxy
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- 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
- C10L1/185—Ethers; Acetals; Ketals; Aldehydes; Ketones
- C10L1/1852—Ethers; Acetals; Ketals; Orthoesters
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- 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
- C10L1/19—Esters ester radical containing compounds; ester ethers; carbonic acid esters
- C10L1/1905—Esters ester radical containing compounds; ester ethers; carbonic acid esters of di- or polycarboxylic acids
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- 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
- C10L2230/00—Function and purpose of a components of a fuel or the composition as a whole
- C10L2230/22—Function and purpose of a components of a fuel or the composition as a whole for improving fuel economy or fuel efficiency
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Abstract
The invention discloses the alcohol-based fuel of not smoked eye when using, it is characterised in that is made up of the composition of following weight parts:85.0 95.0 parts of methanol, 2.0 8.0 parts of ethanol, 2.0 5.0 parts of the tert-butyl alcohol, 1.0 2.0 parts of paraffin oil, 0.2 0.5 parts of iron chloride, 0.2 0.5 parts of methyl tertiary butyl ether(MTBE), 0.05 0.1 parts of ethyl acetate, 1.5 2.5 parts of additive;The additive is obtained by following preparation methods:1. pressurized treatments:The loguat leaf residue that water was extracted, is put into pressure pan, is forced into 3kg/cm2, make its pressure uniform, maintain, then abrupt release pressure;2. distillation is handled:1. material that step is obtained is put into distiller, in distiller bottom, heating burning or is passed through steam, and when hot steam is filled in distiller, steam is introduced into condenser by condenser pipe, then passes through oil water separator, collects oil phase;3. high-shear homogenizing machine is handled:2. oil phase that step is obtained is handled by high-shear homogenizing machine, and nano-emulsion is made, and obtains additive.
Description
Technical field
The present invention relates to fuel area, and in particular to the alcohol-based fuel of not smoked eye during use.
Background technology
Alcohol-based fuel is a kind of based on methanol, is mixed with the liquid fuel of the polyalcohols such as ethanol, propyl alcohol and alkane, again
It is named as " methyl fuel ".It is also a kind of biomass energy, is various countries as nuclear energy, solar energy, wind power energy, hydraulic energy
The environment protection clean energy that government widelys popularize at present.The calorific value of alcohol-based fuel typically between 2011-2610MJ/kg, be diesel oil,
60% or so of the exotic fuels calorific value such as liquefied gas, belongs to low heat value liquid fuel, and alcohol-based fuel can be with water in any proportion
It is mutually dissolved, but does not form azeotropic mixture with water, the calorific value of aqueous fuel will be lower.
The research of present alcohol-based fuel is a lot, such as Chinese patent CN102625825A, discloses a kind of methanol-based liquid combustion
The production method of material, methods described include:By the methanol of 55-80% by volume, by volume 23-50% water and by volume
The accelerator for counting 2-5% is mixed to form premix, the height for then making premix be subjected in mechanical high frequency ultrasound reactor
Frequency sonic oscillation, is added after that the catalyst of 3%-5% by volume, then makes premix by pressure filter,
It is finally set to seal at least 48 hours, so as to produce liquid fuel.The ratio of formula reclaimed water can at most account for 50%, it is possible to understand that
For " water becomes oil ".And for example Chinese patent CN103184081A, a kind of alcohol-group fuel oil is disclosed, by the component group of following parts by weight
Into:Methanol 70-75 parts, dimethylbenzene 4-6 parts, No. 200 solvent naphtha 4-6 parts, paraffin oil 4-6 parts, glycerine 4-6 parts, water 5-10 parts.But
It is that there is also deficiency, adds water in order to reduce cost so that methanol content makes fuel value very below 75% in fuel
It is low.Although in alcohol radical liquid fuel, appropriate water can be contained, it is aqueous to improve flash temperature, the danger caught fire is reduced,
It is that moisture is mixed into fuel, two aspects is shown to metal erosion:First, moisture can directly cause the chemical nuclear power of metal
Learn corrosion;Second, as some sulfur-bearing and sour corrosion materials in fuel be dissolved in water when, then accelerate corrosion of metal process.
Harm of the free water to metal in fuel is very big, and it can corrode various steel components.As steel oil tank, oil drum, pipeline, valve and
Other parts.The micro-moisture being dissolved in fuel can only cause low content steel corrosion.Moisture has stronger to low-alloy steel
Corrosiveness, also corrode the non-ferrous metal such as copper and zinc, corrosion is not produced to bronze.Chinese patent CN103923709A, improving
While the content of methanol, the content of moisture is reduced, but in reality in use, it has also been found that some problems, for example, product
In without specialist additive is added, cause fuel insufficient, black smoke, carbon distribution, black-cooking pot bottom be present, no raffinate residue, in use
There is the problems such as smoked people, dazzling.
In the prior art, many alcohol-based fuel producers declare to the addition of stabilizer, emulsifying agent in fuel, calorific value after burning
Height, discharge amount of exhaust gas are extremely low.Although some manufacturing enterprises boast fantastically the emulsifying agent added, actually various
The so-called stabilizer being exclusively formulated, emulsifying agent are often the mixture of the chemicals such as flavor enhancement, coloring agent, metal ion, and one
As be all 6-9 kinds industrial chemicals dissolving after mixing liquid, the relation with environmental emission reduction in combustion process is not too big.Part
Producer declares to have it is possible to additionally incorporate additive in alcohol-based fuel to improve calorific value, can greatly improve the calorific value of fuel.
But in fact, unless disregard into local other fuel for adding high heating value, otherwise, only add based on all kinds of industrial chemicals
Additive alcohol-based fuel low heat value can only be made to be changed in a small range, the alcohol-based fuel low heat value after adjustment is difficult often
Break through 27MJ/kg.In actual use, rear kitchen personnel not only have carbon distribution after generally reflecting fuel combustion, and flue gas is smoked
Eye, it is necessary to force air draft ability normal work with blower fan, problem is still present.
The content of the invention
The purpose of the present invention is overcome the deficiencies in the prior art, there is provided the alcohol-based fuel of not smoked eye during use, during the use
The alcohol-based fuel of not smoked eye can be used for external-burning combustion field, alternative diesel oil and traditional fuel oil.
To reach above-mentioned purpose, the present invention is achieved through the following technical solutions, the alcohol-based fuel of not smoked eye during use
It is made up of the composition of following weight parts:
The additive is obtained by following preparation methods:
1. pressurized treatments:The loguat leaf residue that water was extracted, is put into pressure pan, is forced into 3kg/cm2, make its pressure
Uniformly, maintain, then abrupt release pressure;
2. distillation is handled:1. material that step is obtained is put into distiller, in distiller bottom, heats burning or is passed through steaming
Vapour, when hot steam is filled in distiller, steam is introduced into condenser by condenser pipe, then by oil water separator,
Collect oil phase;
3. high-shear homogenizing machine is handled:2. oil phase that step is obtained is handled by high-shear homogenizing machine, and nano-emulsion is made,
Obtain additive.
It is of the present invention to make its pressure uniform, maintain, then abrupt release pressure, preferably makes its pressure uniform, maintains
5-10min, pressure is then discharged in 1-5s.
High-shear homogenizing machine processing of the present invention, preferred linear velocity 30-40m/s, time 3-5min.
In the present invention, ethanol, the tert-butyl alcohol are added, calorific value can be increased, reach good combustion efficiency, while can change
The proportion of alcohol-based fuel.
The tert-butyl alcohol, iron chloride improve alcohol-based fuel calorific value, flameholding, easily igniting, burning are imitated as combustion-supporting gain of heat agent
Rate is high.
The proportion of paraffin oil is lighter than methanol, and boiling point is very high about 110 DEG C, and paraffin oil will not be dissolved by methanol, methanol
Directly being contacted with air to be volatilized, and iron chloride is added in the present invention and can be very good to avoid such case, can improve alcohol radical combustion
Intersolubility in material system, prevent from being layered so that paraffin oil and methanol in alcohol-based fuel are combined closely, and are dodged so as to reach to improve
The purpose of point, it is contemplated that cost factor, paraffin oil addition should not be too big.
Ethyl acetate, as corrosion inhibitor, by physical absorption film forming or chemisorbed membrane formation mechanism to iron, copper, aluminium
Corrosion Deng black, non-ferrous metal forms inhibitory action, particularly controls hydroxyl corrosion, while suppress to parts such as rubber
Corrosion, extend the maintenance cycle of equipment.
Methyl tertiary butyl ether(MTBE), as stabilizer, octane number and Cetane number are effectively improved, make burning more stable, can be
Initial Stage after Ignition increases fulminant burning, makes igniting easy, the problem for solving cold-starting.Overcome vapour lock problem.
Compared with prior art, the advantage of the invention is that:
1st, in the prior art, some producers add dimethyl ether (DEM) and higher alcohols as additive, but not only need multiple
It miscellaneous technique, also can greatly improve the production cost of alcohol-based fuel.And the additive arrived of the present invention, have to belong to and compare water
Gently, calorific value height, safety and environmental protection, difficult volatilization, flammable but nonflammable, energy completely burned noresidue oil-based liquid organic matter, as
The additive of alcohol-based fuel, it is very suitable.
2nd, prior art, usually simple not only reduces alcohol radical combustion by addition calorific value enhancer, increase hydrocarbon content
The security performance of material, and the rising of alcohol-based fuel cost price is result in, it is unfavorable for the popularization of alcohol-based fuel.The addition of the present invention
Agent, it, which is acted on, mainly functionally improves fuel combustion operating mode, such as reduces consumption, increase flammability, security, reduces corrosion
Property, flue gas when preventing from using smokes eye.Moreover, the additive of the present invention have passed through high-shear homogenizing machine processing, with nano-emulsion
Form adds alcohol-based fuel as additive, is that obtained alcohol-based fuel is easily atomized, vaporizes, evaporated.
3rd, additive of the invention derives from the residue of plant extracts, many plant extracts, after entering water extraction, one
As be as offal treatment, it is and of the invention, especially choose the plant residue after water extraction, it is residual compared to the plant after alcohol extracting
Slag, there is the liposoluble constituent such as substantial amounts of essential oil to exist in the plant residue after water extraction, day of the present invention passes through pressurized treatments, steamed
Processing, high-shear homogenizing machine processing are evaporated, the plants essential oil in residue after vegetation water is extracted can be fully discharged, accomplish to waste
Utilize, kill two birds with one stone.
Embodiment
With embodiment, the invention will be further described below, but the invention is not limited in these embodiments.
Embodiment 1:
The alcohol-based fuel of not smoked eye when using is prepared, according to following components and ratio mixing (stirring at room temperature)
The alcohol-based fuel of not smoked eye when obtaining using:
The additive is obtained by following preparation methods:
1. pressurized treatments:The loguat leaf residue that water was extracted, is put into pressure pan, is forced into 3kg/cm2, make its pressure
Uniformly, 5-10min is maintained, pressure is then discharged in 1-5s;
2. distillation is handled:1. material that step is obtained is put into distiller, in distiller bottom, heats burning or is passed through steaming
Vapour, when hot steam is filled in distiller, steam is introduced into condenser by condenser pipe, then by oil water separator,
Collect oil phase;
3. high-shear homogenizing machine is handled:2. oil phase that step is obtained is handled by high-shear homogenizing machine, linear velocity 30-
40m/s, time 3-5min, is made nano-emulsion, obtains additive.
Embodiment 2:
The alcohol-based fuel of not smoked eye when using is prepared, according to following components and ratio mixing (stirring at room temperature)
The alcohol-based fuel of not smoked eye when obtaining using:
The additive is obtained by following preparation methods:
1. pressurized treatments:The loguat leaf residue that water was extracted, is put into pressure pan, is forced into 3kg/cm2, make its pressure
Uniformly, 5-10min is maintained, pressure is then discharged in 1-5s;
2. distillation is handled:1. material that step is obtained is put into distiller, in distiller bottom, heats burning or is passed through steaming
Vapour, when hot steam is filled in distiller, steam is introduced into condenser by condenser pipe, then by oil water separator,
Collect oil phase;
3. high-shear homogenizing machine is handled:2. oil phase that step is obtained is handled by high-shear homogenizing machine, linear velocity 30-
40m/s, time 3-5min, is made nano-emulsion, obtains additive.
Embodiment 3:
The alcohol-based fuel of not smoked eye when using is prepared, according to following components and ratio mixing (stirring at room temperature)
The alcohol-based fuel of not smoked eye when obtaining using:
The additive is obtained by following preparation methods:
1. pressurized treatments:The loguat leaf residue that water was extracted, is put into pressure pan, is forced into 3kg/cm2, make its pressure
Uniformly, 5-10min is maintained, pressure is then discharged in 1-5s;
2. distillation is handled:1. material that step is obtained is put into distiller, in distiller bottom, heats burning or is passed through steaming
Vapour, when hot steam is filled in distiller, steam is introduced into condenser by condenser pipe, then by oil water separator,
Collect oil phase;
3. high-shear homogenizing machine is handled:2. oil phase that step is obtained is handled by high-shear homogenizing machine, linear velocity 30-
40m/s, time 3-5min, is made nano-emulsion, obtains additive.
Comparative example 1:
Alcohol-based fuel is prepared, alcohol-based fuel is obtained according to following components and ratio mixing (stirring at room temperature):
Comparative example 2:
Alcohol-based fuel is prepared, alcohol-based fuel is obtained according to following components and ratio mixing (stirring at room temperature):
The additive is obtained by following preparation methods:
1. pressurized treatments:The loguat leaf residue that water was extracted, is put into pressure pan, is forced into 3kg/cm2, make its pressure
Uniformly, 5-10min is maintained, pressure is then discharged in 1-5s;
2. distillation is handled:1. material that step is obtained is put into distiller, in distiller bottom, heats burning or is passed through steaming
Vapour, when hot steam is filled in distiller, steam is introduced into condenser by condenser pipe, then by oil water separator,
Oil phase is collected, obtains additive.
Experimental example:
Combustion characteristics Experimental comparison's research is carried out to embodiment 3, the alcohol-based fuel of comparative example, 0# diesel oil.Fuel oil passes through
Pipeline enters combustion chambers burn by burner nozzle, heats 20kg water, and water temperature is from 40 DEG C to 80 DEG C, and air is by air blower from combustion
Combustor side walls drum people combustion chamber, flue gas caused by burning is discharged into air by flue, and extracts flue gas with smoke sampling device and pass through cigarette
The qi leel analyzer measurement (average value of test data when the numerical value of flue gas is 40 DEG C, 50 DEG C, 60 DEG C, 70 DEG C, 80 DEG C, by relatively empty
Gas consumption coefficient is that 1.1 conversions draw alcohol-based fuel burning, the relative amount of diesel combustion smoke components).
By document, it is 45% to calculate alcohol-based fuel combustion thermal efficiency, and the diesel combustion thermal efficiency is 26%, Ke Yifa
Existing alcohol-based fuel combustion thermal efficiency is significantly larger than the diesel combustion thermal efficiency, and the unit mass calorific value (14-27MJ/ of alcohol-based fuel
Kg) far below fossil fuel energies such as the diesel oil (42.9MJ/kg) of people's custom.From upper table it can be found that because diesel oil calorific value is
2 times or so of alcohol-based fuel calorific value, heating water temperature to same temperature, the time required for the burning alcohol-based fuel of embodiment 3 is only
0.71 times the time required to being only burning diesel oil, the fuel consumption of the alcohol-based fuel of embodiment 3 is 1.74 times of diesel oil fuel consumption, with reference to
Diesel oil, the alcohol-based fuel of embodiment 3 into seeing originally, use the alcohol-based fuel of embodiment 3 on the premise of same effectively heat energy is obtained
More economically.
By embodiment 3 and comparative example 1, the comparison of comparative example 2, compare from time and fuel consumption, have 5-8% left
Right lifting, reason are that the additive of embodiment 3 have passed through high-shear homogenizing machine processing, addition are used as in the form of nano-emulsion
Agent add alcohol-based fuel, so as to get alcohol-based fuel be easily atomized, vaporize, evaporate, meanwhile, reduce CO generation, also improve
Smoked eye, dazzling problem when using.
Claims (3)
1. the alcohol-based fuel of not smoked eye when using, it is characterised in that be made up of the composition of following weight parts:
The additive is obtained by following preparation methods:
1. pressurized treatments:The loguat leaf residue that water was extracted, is put into pressure pan, is forced into 3kg/cm2, make its pressure uniform,
Maintain, then abrupt release pressure;
2. distillation is handled:1. material that step is obtained is put into distiller, in distiller bottom, heats burning or is passed through steam,
When hot steam is filled in distiller, steam is introduced into condenser, then by oil water separator, receive by condenser pipe
Collect oil phase;
3. high-shear homogenizing machine is handled:2. oil phase that step is obtained is handled by high-shear homogenizing machine, and nano-emulsion is made, and is obtained
Additive.
2. the alcohol-based fuel of not smoked eye during a kind of use according to claim 1, it is characterised in that:Described makes its pressure
Uniformly, maintain, then abrupt release pressure, is to make its pressure uniform, maintains 5-10min, pressure is then discharged in 1-5s.
3. the alcohol-based fuel of not smoked eye during use according to claim 1, it is characterised in that:Described high-shear homogenizing machine
Processing, linear velocity 30-40m/s, time 3-5min.
Priority Applications (1)
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