CN107903952A - A kind of alcohol-based fuel - Google Patents

A kind of alcohol-based fuel Download PDF

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Publication number
CN107903952A
CN107903952A CN201711167144.6A CN201711167144A CN107903952A CN 107903952 A CN107903952 A CN 107903952A CN 201711167144 A CN201711167144 A CN 201711167144A CN 107903952 A CN107903952 A CN 107903952A
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CN
China
Prior art keywords
alcohol
steam
based fuel
handled
parts
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
Application number
CN201711167144.6A
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Chinese (zh)
Inventor
粟健林
陶积勇
卢昌锐
曾庆发
张光学
周顺
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Liuzhou Shun Ze Environmental Protection Technology Co Ltd
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Liuzhou Shun Ze Environmental Protection Technology 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.)
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Publication date
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Priority to CN201711167144.6A priority Critical patent/CN107903952A/en
Publication of CN107903952A publication Critical patent/CN107903952A/en
Pending legal-status Critical Current

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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
    • C10L1/02—Liquid carbonaceous fuels essentially based on components consisting of carbon, hydrogen, and oxygen only
    • 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
    • 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
    • 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
    • C10L1/1233—Inorganic compounds oxygen containing compounds, e.g. oxides, hydroxides, acids and salts thereof
    • C10L1/125—Inorganic compounds oxygen containing compounds, e.g. oxides, hydroxides, acids and salts thereof water
    • 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
    • C10L1/16—Hydrocarbons
    • 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
    • C10L1/1802—Organic compounds containing oxygen natural products, e.g. waxes, extracts, fatty oils
    • 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
    • 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
    • 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
    • C10L1/185—Ethers; Acetals; Ketals; Aldehydes; Ketones
    • C10L1/1857—Aldehydes; Ketones

Landscapes

  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Liquid Carbonaceous Fuels (AREA)

Abstract

The invention discloses a kind of alcohol-based fuel, is made of the component of following weight parts：85.0 96.0 parts of methanol, 2.0 6.0 parts of ethanol, 1.0 5.0 parts of butanone, 1.0 2.0 parts of paraffin oil, 0.5 2.0 parts of water, 0.1 0.2 parts of iron chloride, 1.0 2.0 parts of additive；The additive is obtained by following preparation methods：1. Steam explosion treatment：The cape jasmine residue that water was extracted, is put into the processing of steam blasting tank；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

A kind of alcohol-based fuel
Technical field
The present invention relates to fuel area, and in particular to a kind of alcohol-based fuel.
Background technology
Alcohol-based fuel is exactly the fuel configured using alcohols (such as methanol, ethanol, butanol) material as main body.It is with liquid Or existing for solid form.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.In face of the exhaustion of fossil energy, alcohol-based fuel is most potential new replaces It is deep to be favored by every industry or trade's tissue for the energy.
The research of present alcohol-based fuel is very much, such as Chinese patent CN103184081A, discloses a kind of alcohol-group fuel oil, by The component composition of following parts by weight：70-75 parts of methanol, 4-6 parts of dimethylbenzene, No. 200 4-6 parts of solvent naphthas, 4-6 parts of paraffin oil are sweet It is 4-6 parts oily, 5-10 parts of water.But Shortcomings, first, dimethylbenzene has toxicity, secondly, adds water in order to reduce cost, So that methanol content makes fuel value very low below 75% in fuel.Although in alcohol radical liquid fuel, can contain suitable Water, it is aqueous to improve flash temperature, the danger caught fire is reduced, but moisture is mixed into fuel, two are shown to metal erosion A aspect：First, moisture can directly cause the chemical nuclear power chemical attack of metal；Second, such as some sulfur-bearings and acidity in fuel When corrosive deposit is dissolved in water, then accelerate corrosion of metal process.Harm of the free water to metal in fuel is very big, its energy Corrode various steel components, such 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 low-alloy steel stronger corrosiveness, also corrodes the non-ferrous metal such as copper and zinc, to green grass or young crops Copper does not produce corrosion.And for example Chinese patent CN103911189A, while the content of methanol is improved, reduces containing for moisture Amount, but actual in use, it has also been found that some problems, for example, no in product add specialist additive, cause fuel not Fully, there are black smoke, carbon distribution, black-cooking pot bottom, there is the problems such as smoked people, dazzling in use in no raffinate residue.
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 the dissolved mixing liquid of 6-9 kind industrial chemicals, 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 change 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 to work normally with wind turbine, problem still remains.
The content of the invention
The purpose of the present invention is overcoming the deficiencies of the prior art and provide a kind of alcohol-based fuel, alcohol-based fuel combustion can be improved Environment after burning, the alcohol-based fuel 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, a kind of alcohol-based fuel, by following weight The component of part is made：
The additive is obtained by following preparation methods：
1. Steam explosion treatment：The cape jasmine residue that water was extracted, is put into the processing of steam blasting tank；
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.
Of the present invention to be put into the processing of steam blasting tank, preferably burst pressure 3.0-3.5Mpa, the dwell time maintains 150-200s。
High-shear homogenizing machine processing of the present invention, preferred linear velocity 30-40m/s, time 3-5min.
In the present invention, ethanol, butanone are added, calorific value can be increased, reach good combustion efficiency, while alcohol can be changed The proportion of base fuel.The proportion of paraffin oil is lighter than methanol, and boiling point is very about 110 DEG C, and paraffin oil will not be dissolved by methanol high, Methanol is directly contacted with air to volatilize, and iron chloride is added in the present invention and can be very good to avoid such case, can improve alcohol Intersolubility in base fuel system, prevents from being layered so that paraffin oil and methanol in alcohol-based fuel are combined closely, and are carried so as to reach The purpose of high-flash, it is contemplated that cost factor, paraffin oil additive amount should not be too big.
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 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, is very suitable.
2nd, the prior art, is usually that calorific value enhancer is added in simple relying on, increase hydrocarbon content not only reduces alcohol radical combustion 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, reduce 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, and the alcohol-based fuel for being easily is atomized, vaporizes, evaporates.
3rd, additive of the invention derives from the residue of plant extracts, many plant extracts, into after crossing 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, also has the liposoluble constituent such as substantial amounts of essential oil to exist in the plant residue after water extraction, day of the present invention by steam blasting at Reason, distillation processing, high-shear homogenizing machine processing, can fully discharge the plants essential oil in residue after vegetation water is extracted, accomplish To waste utilization, 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：
Alcohol-based fuel is prepared, alcohol-based fuel is obtained according to following components and ratio mixing (stirring evenly at room temperature)：
The additive is obtained by following preparation methods：
1. Steam explosion treatment：The cape jasmine residue that water was extracted, is put into steam blasting tank, burst pressure 3.0- 3.5Mpa, dwell time maintain 150-200s；
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：
Alcohol-based fuel is prepared, alcohol-based fuel is obtained according to following components and ratio mixing (stirring evenly at room temperature)：
The additive is obtained by following preparation methods：
1. Steam explosion treatment：The cape jasmine residue that water was extracted, is put into steam blasting tank, burst pressure 3.0- 3.5Mpa, dwell time maintain 150-200s；
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：
Alcohol-based fuel is prepared, alcohol-based fuel is obtained according to following components and ratio mixing (stirring evenly at room temperature)：
The additive is obtained by following preparation methods：
1. Steam explosion treatment：The cape jasmine residue that water was extracted, is put into steam blasting tank, burst pressure 3.0- 3.5Mpa, dwell time maintain 150-200s；
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 evenly at room temperature)：
Comparative example 2：
Alcohol-based fuel is prepared, alcohol-based fuel is obtained according to following components and ratio mixing (stirring evenly at room temperature)：
The additive is obtained by following preparation methods：
1. Steam explosion treatment：The cape jasmine residue that water was extracted, is put into steam blasting tank, burst pressure 3.0- 3.5Mpa, dwell time maintain 150-200s；
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：
Alcohol-based fuel, 0# diesel oil to embodiment 3, comparative example carry out combustion characteristics Experimental comparison's research.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, the flue gas for generation of 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 draws alcohol-based fuel burning, the relative amount of diesel combustion smoke components for 1.1 conversions).
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 since diesel oil calorific value is 2 times or so of alcohol-based fuel calorific value, heating water temperature to same temperature, embodiment 3 burn the alcohol-based fuel required time only 0.67 times the time required to being only burning diesel oil, the fuel consumption of 3 alcohol-based fuel of embodiment is 1.65 times of diesel oil fuel consumption, with reference to Diesel oil, 3 alcohol-based fuel of embodiment into seeing originally, use 3 alcohol-based fuel of embodiment on the premise of same effectively thermal energy is obtained More economically.
By embodiment 3 and comparative example 1, the comparison of comparative example 2, compare from time and fuel consumption, there is 8-10% The lifting of left and right, reason is that the additive of embodiment 3 have passed through high-shear homogenizing machine processing, as adding in the form of nano-emulsion Add agent add alcohol-based fuel, so as to get alcohol-based fuel be easily atomized, vaporize, evaporate, meanwhile, reduce the generation of CO, also change Smoked eye, dazzling problem when being apt to use.

Claims (3)

  1. A kind of 1. alcohol-based fuel, it is characterised in that：It is made of the component of following weight parts：
    The additive is obtained by following preparation methods：
    1. Steam explosion treatment：The cape jasmine residue that water was extracted, is put into the processing of steam blasting tank；
    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. A kind of 2. alcohol-based fuel according to claim 1, it is characterised in that：The steam blasting tank that is put into is handled, quick-fried Broken pressure 3.0-3.5Mpa, dwell time maintain 150-200s.
  3. A kind of 3. alcohol-based fuel according to claim 1, it is characterised in that：The high-shear homogenizing machine processing, linear speed Spend 30-40m/s, time 3-5min.
CN201711167144.6A 2017-11-21 2017-11-21 A kind of alcohol-based fuel Pending CN107903952A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201711167144.6A CN107903952A (en) 2017-11-21 2017-11-21 A kind of alcohol-based fuel

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201711167144.6A CN107903952A (en) 2017-11-21 2017-11-21 A kind of alcohol-based fuel

Publications (1)

Publication Number Publication Date
CN107903952A true CN107903952A (en) 2018-04-13

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Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1493669A (en) * 2002-10-29 2004-05-05 符树庆 Vegeteble oil derivative liqid fuel oil environmental protection energy saving additive
US20060201056A1 (en) * 2000-04-14 2006-09-14 Oryxe Energy International, Inc. Biodiesel fuel additive
CN103265981A (en) * 2013-05-20 2013-08-28 清远市精旺环保设备有限公司 Alcohol-based fuel combustion improver and alcohol-based fuel
CN103911189A (en) * 2014-04-10 2014-07-09 桂林市淦隆环保科技有限公司 Alcohol-based fuel

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20060201056A1 (en) * 2000-04-14 2006-09-14 Oryxe Energy International, Inc. Biodiesel fuel additive
CN1493669A (en) * 2002-10-29 2004-05-05 符树庆 Vegeteble oil derivative liqid fuel oil environmental protection energy saving additive
CN103265981A (en) * 2013-05-20 2013-08-28 清远市精旺环保设备有限公司 Alcohol-based fuel combustion improver and alcohol-based fuel
CN103911189A (en) * 2014-04-10 2014-07-09 桂林市淦隆环保科技有限公司 Alcohol-based fuel

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
张晓阳等: "《纤维素生物质水解与应用》", 31 December 2012, 郑州大学出版社 *

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Application publication date: 20180413