CN1422934A - Micro emulsion fuel production process and formula - Google Patents
Micro emulsion fuel production process and formula Download PDFInfo
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- CN1422934A CN1422934A CN 01138773 CN01138773A CN1422934A CN 1422934 A CN1422934 A CN 1422934A CN 01138773 CN01138773 CN 01138773 CN 01138773 A CN01138773 A CN 01138773A CN 1422934 A CN1422934 A CN 1422934A
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- emulsifying agent
- emulsified fuel
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Abstract
The invention is a producing technique of micro-emulsified fuel and the formula. Its character: according to the weight percentage, emulsifying agent 6-9%, fuel 70-80%, purified water 15-20% and assistant 0.4-0.7%, mix them and fully stir to make the micro-emulsifier fuel. It adopts the micro-emulsifier techinque. It can alone be used and also mixed with similar fuel for use.
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
For saving oil, have the production technique of various emulsified fuels or petroleum supplements and prescription to come out one after another at present, but its product, no matter after calorific value, production cost, the burning in the tail gas objectionable constituent content, colourity etc. all not ideal enough,
Summary of the invention
The object of the invention just provides a kind of production technique and prescription of micro-emulsified fuel, makes the emulsified fuel cost low, and objectionable constituent content is low in the tail gas of burning back, the micro-emulsified fuel of economical and environment-friendly type.
Production technique of the present invention and prescription be, with emulsifying agent, purify waste water, auxiliary agent, kerosene or diesel oil mixes and fully stir and form, its each component is by weight ratio, emulsifying agent is 6-9%, purifying waste water is that 10-20%, auxiliary agent are 0.4-0.9%, and kerosene or diesel oil are 70-80%.Emulsifying agent is to be mixed and fully stirred by sapn, tween, peregal, oleic acid, naphthenic acid to form in about 10 minutes, and its weight proportion is, sapn is 7-15%, and tween is 1-4%, and the average 1-4% that adds as, oleic acid are 1-2%, and naphthenic acid is 75-90%.Auxiliary agent is to be mixed by Virahol and quadrol, and fully stirs about 10 minutes and form, and its weight proportion is, Virahol is 10-40%, and quadrol is 60-90%.Purifying waste water is to sneak into 8 ‰ alkali in water, and fully stirs about 10 minutes formulated.
At normal temperatures and pressures, by proportioning emulsifying agent is mixed with kerosene or diesel oil, and fully stir about 20 minutes, add again and purify waste water, fully stir again about 20 minutes, add auxiliary agent again, after fully stirring about 20 minutes again, just make microemulsified kerosene or micro emulsion diesel fuel.
Because what the present invention adopted is micro-emulsion technology, form the short grained water-in-oil shape of 0.005-0.02 μ m solution, this solution micella grain has reached nano level, less than wavelength of visible light, so micellar solution is transparent, between the profit no interface, also there is not interfacial tension.Its product free from extraneous odour, not stratified, do not precipitate, sufficient combustion, production cost are low, objectionable constituent content is low in the tail gas after the burning, this product can use separately also can mix with similar oil and use.
Description of drawings
Accompanying drawing is the technological process of production figure of micro-emulsified fuel.
Embodiment
Example 1, the proportioning of microemulsified kerosene, by weight, kerosene is 76%, and emulsifying agent is 8.25%, and purifying waste water is 15%, and auxiliary agent is 0.75%.Emulsifying agent is by weight ratio, and sapn is 12.7%, and tween is 3.6%, and oil is 1.8%, and cycloalkanes is 81.9%.
Example 2, the proportioning of micro emulsion diesel fuel, by weight, diesel oil is 76%, and emulsifying agent is 8.75%, and purifying waste water is 15%, and auxiliary agent is 0.75%.Emulsifying agent is by weight ratio, and sapn is 12.7%, and tween is 1.8%, averagely adds as 1.8%, and oil is 1.8%, and cycloalkanes is 81.9%.
Claims (5)
1, a kind of production technique of micro-emulsified fuel and prescription, it is characterized in that by weight ratio, emulsifying agent is that 6-9% is that 70-80% mixes mutually with fuel oil, fully stir about 20 minutes at normal temperatures, again with purify waste water to 15-20% mixes mutually, and fully stir about 20 minutes, be that 0.4-0.7% mixes mutually with auxiliary agent again, and fully stir about 20 minutes, make micro-emulsified fuel.
2, the production technique of a kind of micro-emulsified fuel according to claim 1 and prescription, it is characterized in that emulsifying agent by weight ratio, sapn is 7-15%, tween is 1-4%, the average 1-4% that adds as, oleic acid is 1-2%, and naphthenic acid is that 75-90% mixes mutually, and fully stirs about 10 minutes and make emulsifying agent.
3, the production technique of a kind of micro-emulsified fuel according to claim 1 and prescription is characterized in that in water adding 8 ‰ alkali, purify waste water through fully mixing to make about 10 minutes.
4, the production technique of a kind of micro-emulsified fuel according to claim 1 and prescription is characterized in that auxiliary agent by weight ratio, and Virahol is that 10-40% and quadrol are 60-90%, through mixing, and fully stir about 10 minutes and make auxiliary agent.
5, the production technique of a kind of micro-emulsified fuel according to claim 1 and prescription is characterized in that micro-emulsified fuel best proportioning by weight is, fuel oil is 76%, and emulsifying agent is 8.25%, and purifying waste water is 15%, and auxiliary agent is 0.75%; The best by weight proportioning of emulsifying agent is, sapn is 12.7%, and tween is 1.8-3.6%, and the average 0-1.8% that adds as, oleic acid are 1.8%, and naphthenic acid is 81.9%.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN 01138773 CN1422934A (en) | 2001-12-06 | 2001-12-06 | Micro emulsion fuel production process and formula |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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CN 01138773 CN1422934A (en) | 2001-12-06 | 2001-12-06 | Micro emulsion fuel production process and formula |
Publications (1)
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CN1422934A true CN1422934A (en) | 2003-06-11 |
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CN 01138773 Pending CN1422934A (en) | 2001-12-06 | 2001-12-06 | Micro emulsion fuel production process and formula |
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2004094570A1 (en) * | 2003-04-23 | 2004-11-04 | Wenhao Wang | A nano-granule fuel and its preparation |
CN1304536C (en) * | 2003-08-20 | 2007-03-14 | 龚龑 | Nanometer micro-emulsified fuel oil synergist and preparing method thereof |
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 |
-
2001
- 2001-12-06 CN CN 01138773 patent/CN1422934A/en active Pending
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2004094570A1 (en) * | 2003-04-23 | 2004-11-04 | Wenhao Wang | A nano-granule fuel and its preparation |
EA007625B1 (en) * | 2003-04-23 | 2006-12-29 | Вэнхао Ванг | A nano-granule fuel oil and method for preparing thereof |
US7909996B2 (en) | 2003-04-23 | 2011-03-22 | Wenhao Wang | Nano-granule fuel and its preparation |
CN1304536C (en) * | 2003-08-20 | 2007-03-14 | 龚龑 | Nanometer micro-emulsified fuel oil synergist and preparing method thereof |
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 |
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Legal Events
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C06 | Publication | ||
PB01 | Publication | ||
C02 | Deemed withdrawal of patent application after publication (patent law 2001) | ||
WD01 | Invention patent application deemed withdrawn after publication |