CN1410514A - Production technology and formulation of microemulsion fuel oil - Google Patents
Production technology and formulation of microemulsion fuel oil Download PDFInfo
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- CN1410514A CN1410514A CN 02133065 CN02133065A CN1410514A CN 1410514 A CN1410514 A CN 1410514A CN 02133065 CN02133065 CN 02133065 CN 02133065 A CN02133065 A CN 02133065A CN 1410514 A CN1410514 A CN 1410514A
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Abstract
A microemulsified fuel oil is prepared from fatty acid (or oleic acid) (15 vol.%), triethanolamine (or biethanolamine) (2 vol.%), isopentanol (3 vol.%), water (20 vol.%) and diesel oil (60 vol.%). Its advantages are low cost, little harmful gas, and long service life of diesel engine.
Description
Affiliated field
The invention belongs to the production technique and the prescription in fuel oil field, particularly a kind of emulsified fuel.
Background technology
Oil is the non-renewable energy, for saving oil, there are the production technique and the prescription of the fuel substitute of various emulsified fuels and oil to come out one after another at present, but the every technical indicator of its product, as calorific value, tail gas oxious component content, cost, colourity etc., all not out of this world.Find through further investigation, in the material oily, that the water two-phase is immiscible, add a large amount of tensio-active agent and cosurfactant, make the surface tension of oil, water reduce to extremely low, even reduce to negative value in moment, make whole system spontaneously form translucent or transparent isotropic liquid system, water is dispersed in as disperse phase and forms the W/O microemulsion in the oil, and the liquid pearl radius of this microemulsion is generally 10-100nm, thermodynamics is highly stable, not stratified, do not precipitate, high temperature resistant, easy storage.Tensio-active agent in the prescription of emulsified fuel, to performance, the cost of its product, influence is very big, thinks through experimental study for many years, adopt the tensio-active agent of the tankage generation of the wide vegetable oil production in source, can reduce fuel cost and can improve the fuel oil technical feature again.
Summary of the invention
Purpose of the present invention just provides micro emulsion fuel production process and the prescription that a kind of technology is simple, equipment simple, the tensio-active agent raw material sources are wide, cost is low, product performance index is all excellent.
Production technique of the present invention is: drop into diesel oil, water, lipid acid in the reactor in proportion, 50-60 ℃ of temperature fully stirred 8-12 minute under normal pressure, add trolamine and primary isoamyl alcohol more in proportion, fully stirred again 8-10 minute, promptly can be made into the micro-emulsified fuel finished product.Its each proportion of raw materials (long-pending ratio) is: lipid acid is 10-20%, and trolamine is that 1-2% primary isoamyl alcohol (C=5) is 2-3%, water-oil ratio 1: 3
The simple equipment used of technology of the present invention is simple, raw material sources are wide, utilize the tankage after the vegetable oil production to be emulsifying agent, tensio-active agent, the every index and the ordinary diesel oil of product are close substantially, calorific value reaches the 9000-9300 kilocalorie, cost reduces about 15-20% than ordinary diesel oil, environment protecting is obvious, compare exhaust smoke level with diesel oil and reduce approximately 60%, it is about 50% that obnoxious flavour reduces, and diesel engine is not had corrosion, can reduce carbon distribution, reduce diesel engine operating temperature and noise, prolong diesel engine work-ing life, the tankage of China's vegetable oil production are made full use of.Economic benefit that tool of the present invention is very high and social benefit.
Description of drawings
Accompanying drawing is the technological process of production figure of micro-emulsified fuel
Embodiment
The production technique of micro-emulsified fuel is diesel oil, water, lipid acid to be dropped in the reactor to mix stir about 10 minutes under 50-60 ℃ of temperature normal pressure, drops into trolamine and primary isoamyl alcohol again, and about 10 minutes of restir can go out finished product.By volume, its optimum formula: water is 20%, diesel oil is 60%, lipid acid is 15%, trolamine is 2%, primary isoamyl alcohol is 3%.
Claims (2)
1, the production technique of micro-emulsified fuel and prescription is characterized in that:
A, production technique are: be to drop into diesel oil, water, lipid acid in the reactor in proportion, 50-60 ℃ of temperature fully stirred 8-12 minute under normal pressure, add trolamine and primary isoamyl alcohol more in proportion, fully stirred again 8-10 minute, promptly can be made into the micro emulsion diesel fuel finished product;
The prescription of b, its each raw material (volume ratio) is: lipid acid is 10-20%, and trolamine is 1-2%, and primary isoamyl alcohol is 2-3%, and water is 1: 3 with the diesel oil ratio.
2, the production technique of micro-emulsified fuel according to claim 1 and prescription is characterized in that: its optimum formula: lipid acid is 15%, and trolamine is 2%, and primary isoamyl alcohol is 3%, and water is 20%, and diesel oil is 60%.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN 02133065 CN1410514A (en) | 2002-09-29 | 2002-09-29 | Production technology and formulation of microemulsion fuel oil |
Applications Claiming Priority (1)
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CN 02133065 CN1410514A (en) | 2002-09-29 | 2002-09-29 | Production technology and formulation of microemulsion fuel oil |
Publications (1)
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CN1410514A true CN1410514A (en) | 2003-04-16 |
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CN 02133065 Pending CN1410514A (en) | 2002-09-29 | 2002-09-29 | Production technology and formulation of microemulsion fuel oil |
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Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN100371427C (en) * | 2004-05-27 | 2008-02-27 | 刘有望 | Bio-fuel-oil and process for making same |
CN101067094B (en) * | 2007-06-12 | 2010-06-09 | 广东工业大学 | Preparation process of microemulsified diesel oil |
CN101250431B (en) * | 2008-03-27 | 2011-07-27 | 武汉科技大学 | Micro-emulsified biological diesel and preparation method thereof |
CN102585941A (en) * | 2012-03-06 | 2012-07-18 | 山东京博控股股份有限公司 | Microemulsification diesel fuel and preparation method thereof |
CN101328424B (en) * | 2007-06-22 | 2012-10-31 | 陈金义 | Formula of biomass emulsified diesel oil |
CN103289766A (en) * | 2013-06-19 | 2013-09-11 | 朱觉锦 | Efficient energy-saving emulsified fuel oil |
CN105420093A (en) * | 2014-11-14 | 2016-03-23 | 程叶红 | Biological surfactant microemulsion production system for cosmetics |
CN105647787A (en) * | 2014-11-14 | 2016-06-08 | 程叶红 | Biological surfactant microemulsion production system for cosmetics |
-
2002
- 2002-09-29 CN CN 02133065 patent/CN1410514A/en active Pending
Cited By (16)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN100371427C (en) * | 2004-05-27 | 2008-02-27 | 刘有望 | Bio-fuel-oil and process for making same |
CN101067094B (en) * | 2007-06-12 | 2010-06-09 | 广东工业大学 | Preparation process of microemulsified diesel oil |
CN101328424B (en) * | 2007-06-22 | 2012-10-31 | 陈金义 | Formula of biomass emulsified diesel oil |
CN101250431B (en) * | 2008-03-27 | 2011-07-27 | 武汉科技大学 | Micro-emulsified biological diesel and preparation method thereof |
CN102585941A (en) * | 2012-03-06 | 2012-07-18 | 山东京博控股股份有限公司 | Microemulsification diesel fuel and preparation method thereof |
CN103289766A (en) * | 2013-06-19 | 2013-09-11 | 朱觉锦 | Efficient energy-saving emulsified fuel oil |
CN105482997A (en) * | 2014-11-14 | 2016-04-13 | 程叶红 | Fermentation kettle for biological surface active agent microemulsion production |
CN105420094A (en) * | 2014-11-14 | 2016-03-23 | 程叶红 | Biological surfactant microemulsion production system for food |
CN105420093A (en) * | 2014-11-14 | 2016-03-23 | 程叶红 | Biological surfactant microemulsion production system for cosmetics |
CN105543076A (en) * | 2014-11-14 | 2016-05-04 | 程叶红 | Production system of biological-surfactant microemulsion for food |
CN105543075A (en) * | 2014-11-14 | 2016-05-04 | 程叶红 | Production system for agricultural biological surfactant microemulsion |
CN105543074A (en) * | 2014-11-14 | 2016-05-04 | 程叶红 | Fermentation kettle for producing biological surfactant through microbial fermentation |
CN105543077A (en) * | 2014-11-14 | 2016-05-04 | 程叶红 | Fermenting kettle for producing food-biological surfactant microemulsion |
CN105647787A (en) * | 2014-11-14 | 2016-06-08 | 程叶红 | Biological surfactant microemulsion production system for cosmetics |
CN105420094B (en) * | 2014-11-14 | 2018-08-31 | 三门华迈化工产品有限公司 | Biological surfactant microemulsion production system for food |
CN105420093B (en) * | 2014-11-14 | 2019-01-08 | 三门华迈化工产品有限公司 | Biological surfactant microemulsion production system for cosmetics |
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