CN108219982A - Novel cosolvent method biodiesel synthesis - Google Patents
Novel cosolvent method biodiesel synthesis Download PDFInfo
- Publication number
- CN108219982A CN108219982A CN201611250717.7A CN201611250717A CN108219982A CN 108219982 A CN108219982 A CN 108219982A CN 201611250717 A CN201611250717 A CN 201611250717A CN 108219982 A CN108219982 A CN 108219982A
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- CN
- China
- Prior art keywords
- tetrahydrofuran
- biodiesel
- cosolvent
- catalyst
- novel
- 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.)
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Classifications
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11C—FATTY ACIDS FROM FATS, OILS OR WAXES; CANDLES; FATS, OILS OR FATTY ACIDS BY CHEMICAL MODIFICATION OF FATS, OILS, OR FATTY ACIDS OBTAINED THEREFROM
- C11C3/00—Fats, oils, or fatty acids by chemical modification of fats, oils, or fatty acids obtained therefrom
- C11C3/04—Fats, oils, or fatty acids by chemical modification of fats, oils, or fatty acids obtained therefrom by esterification of fats or fatty oils
- C11C3/10—Ester interchange
-
- 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
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/10—Biofuels, e.g. bio-diesel
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- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- General Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Wood Science & Technology (AREA)
- Liquid Carbonaceous Fuels (AREA)
Abstract
The cosolvent method of novel cosolvent method biodiesel synthesis non-catalytic:Using cosolvent tetrahydrofuran solubilising methanol, this method rapid reaction only needs 5 10 minutes, and reaction condition is mild, and because being not required to catalyst, catalyst need not be all removed in finished product and byproduct glycerine.But tetrahydrofuran is of high cost, and is Poison.To prevent the leakage of tetrahydrofuran, the requirement higher to equipment.
Description
Technical field
Novel cosolvent method biodiesel synthesis
The present invention relates to the biodiesel technology fields of alternative petrifaction diesel, and in particular to a kind of biodiesel synthesis and
Its technical method.
Invention content
Novel cosolvent method biodiesel synthesis
Biodiesel, also known as fatty acid methyl ester are given up with fruit seeds flora conduits milk or animal tallow oil
Edible oil abandoned etc. makees raw material, is obtained with alcohols (methanol ethyl alcohol) through Transesterification.Biodiesel synthesis refers to using all kinds of
Animal and plant fat is raw material, is modified with alcohols materials such as methanol or ethyl alcohol by friendship esterification reaction, it is made to ultimately become for Inner
A kind of fuel that combustion engine uses.Biodiesel has some clear superiorities, and sulfur content is low, can reduce by about 30% sulfur dioxide
With the discharge of sulfide;Biodiesel has preferable greasy property, can reduce the mill of injection pump, engine cylinder body and connecting rod
Damage, extends its service life;Biodiesel has good fuel performance, and the safety used etc. in transport storages
Property is better than petrifaction diesel.In addition, biodiesel is a kind of regenerative resource and a kind of higher energy of degradability.It uses
Biodiesel can reduce CO2 emission and the discharge of air pollutants.
Background technology
Novel cosolvent method biodiesel synthesis
For biodiesel oil product characteristic compared with common diesel, biodiesel has incomparable performance.(1) have excellent
Good environmental protection characteristic.It is mainly manifested in since sulfur content is low in biodiesel so that the discharge of sulfur dioxide and sulfide is low, can
Reduce by about 30% (being 70% when having catalyst);The aromatic series alkane that can be polluted to environment is free of in biodiesel, thus
Exhaust gas is to human body damage less than petrifaction diesel.Detection shows compared with ordinary diesel oil, and 90% sky can be reduced using biodiesel
Gas toxicity, the trouble for reducing by 94% hinder rate;Due to biodiesel oxygen content height, make few, the discharge of carbon monoxide of discharging fume during its burning
Reduce by about 10% (being 95% when having catalyst) compared with diesel oil;The biological degradability of biodiesel is high.(2) have preferable
Cryogenic engine startability.Additive-free cold filter plugging point reaches -20 DEG C.(3) there is preferable greasy property.Mobilize injection pump
The low wear rate of machine cylinder body and connecting rod, service life are long.(4) there is preferable security performance.Due to flash-point height, biodiesel
It is not belonging to dangerous material.Therefore, it is obvious in transport having for use aspects of storage.(5) have good fuel
Energy.Cetane number is high, its flammability is made to be better than diesel oil, and combustion residue makes the use of catalyst and engine motor oil in subacidity
Service life lengthens.(6) there is renewable performance.As regenerative resource, its different from petroleum reserves passes through agricultural and bioscience
The effort of family, can supply will not be exhausted.In summary:Since the carbon dioxide discharged when biodiesel is burnt is far below the plant
Carbon dioxide absorbed in object growth course, so as to improve caused by the discharge of carbon dioxide global warming this have
Evil is in the great environmental problem of the mankind.Thus biodiesel is a kind of real green diesel.As regenerative resource, with petrochemical industry
It is oily different, can be by strengthening developing agricultural, raw material supply is guaranteed, and price is relatively stablized.Oil crops volume increase space is big, adds
Transgenic technology oil plant oil-containing can be made to have certain room for price-cut up to 70% or so.By OPEC, (oil is not defeated for fuel oil supply
Go abroad tissue) control, be more advantageous to the stability and development in international fuel oil market.Meanwhile the discharge of waste oil is reduced, mitigate dirty
The pressure and cost of water process.Waste cooking oil is converted, people's health is ensured, so as to have the function that double environmental protection.
Specific embodiment
Novel cosolvent method biodiesel synthesis
The cosolvent method of non-catalytic:Using cosolvent tetrahydrofuran solubilising methanol, this method rapid reaction only needs 5-10 points
Clock, reaction condition is mild, and because being not required to catalyst, catalyst need not be all removed in finished product and byproduct glycerine.But tetrahydrofuran
It is of high cost, and be Poison.To prevent the leakage of tetrahydrofuran, the requirement higher to equipment.
Claims (1)
1. novel cosolvent method biodiesel synthesis
The cosolvent method of non-catalytic:Using cosolvent tetrahydrofuran solubilising methanol, this method rapid reaction only needs 5-10 minutes,
Reaction condition is mild, and because being not required to catalyst, catalyst need not be all removed in finished product and byproduct glycerine.But tetrahydrofuran cost
Height, and be Poison.To prevent the leakage of tetrahydrofuran, the requirement higher to equipment.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201611250717.7A CN108219982A (en) | 2016-12-22 | 2016-12-22 | Novel cosolvent method biodiesel synthesis |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201611250717.7A CN108219982A (en) | 2016-12-22 | 2016-12-22 | Novel cosolvent method biodiesel synthesis |
Publications (1)
Publication Number | Publication Date |
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CN108219982A true CN108219982A (en) | 2018-06-29 |
Family
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Family Applications (1)
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CN201611250717.7A Pending CN108219982A (en) | 2016-12-22 | 2016-12-22 | Novel cosolvent method biodiesel synthesis |
Country Status (1)
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CN (1) | CN108219982A (en) |
Citations (12)
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---|---|---|---|---|
CN101245251A (en) * | 2007-02-12 | 2008-08-20 | 北京豹之捷石油化工有限公司 | Process for producing biological diesel oil |
CN101250425A (en) * | 2008-04-10 | 2008-08-27 | 中国寰球工程公司 | Method for preparing bio-diesel oil by employing annular-pipe reactor |
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CN101717698A (en) * | 2009-12-10 | 2010-06-02 | 江苏大学 | Preparation method of biodiesel under existence of cosolvent |
CN102154067A (en) * | 2011-02-23 | 2011-08-17 | 李搏 | Method for very quick and continuous preparation of biodiesel at room temperature |
CN102212426A (en) * | 2011-05-17 | 2011-10-12 | 中国林业科学研究院林产化学工业研究所 | Method for preparing biodiesel by grease continuity ester exchange and mixing cosolvent used in method |
CN102816645A (en) * | 2012-09-14 | 2012-12-12 | 天津工业大学 | Continuous preparation method of biodiesel |
CN102942968A (en) * | 2011-08-15 | 2013-02-27 | 厦门鑫烨盛能源科技有限公司 | Alcoholized oil fuel for kitchen and preparation method thereof |
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CN103396883A (en) * | 2013-06-27 | 2013-11-20 | 黄耀江 | Method for preparing biodiesel by utilizing oil plant |
CN103627530A (en) * | 2012-08-21 | 2014-03-12 | 青岛嘉能节能环保技术有限公司 | Method for synthesizing biodiesel by utilizing jatropha curcas oil |
CN103877958A (en) * | 2014-03-12 | 2014-06-25 | 南京大学昆山创新研究院 | Catalyst for preparing biodiesel and preparation method thereof as well as preparation process of biodiesel |
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CN101250425A (en) * | 2008-04-10 | 2008-08-27 | 中国寰球工程公司 | Method for preparing bio-diesel oil by employing annular-pipe reactor |
CN101717698A (en) * | 2009-12-10 | 2010-06-02 | 江苏大学 | Preparation method of biodiesel under existence of cosolvent |
CN102154067A (en) * | 2011-02-23 | 2011-08-17 | 李搏 | Method for very quick and continuous preparation of biodiesel at room temperature |
CN102212426A (en) * | 2011-05-17 | 2011-10-12 | 中国林业科学研究院林产化学工业研究所 | Method for preparing biodiesel by grease continuity ester exchange and mixing cosolvent used in method |
CN102942968A (en) * | 2011-08-15 | 2013-02-27 | 厦门鑫烨盛能源科技有限公司 | Alcoholized oil fuel for kitchen and preparation method thereof |
CN103627530A (en) * | 2012-08-21 | 2014-03-12 | 青岛嘉能节能环保技术有限公司 | Method for synthesizing biodiesel by utilizing jatropha curcas oil |
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CN103242914A (en) * | 2013-05-30 | 2013-08-14 | 广州市特种承压设备检测研究院 | Method for rapidly producing biodiesel from kitchen garbage and produced biodiesel |
CN103396883A (en) * | 2013-06-27 | 2013-11-20 | 黄耀江 | Method for preparing biodiesel by utilizing oil plant |
CN103877958A (en) * | 2014-03-12 | 2014-06-25 | 南京大学昆山创新研究院 | Catalyst for preparing biodiesel and preparation method thereof as well as preparation process of biodiesel |
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