CN1900239A - Reverse magnetic field boiling fuel oil - Google Patents
Reverse magnetic field boiling fuel oil Download PDFInfo
- Publication number
- CN1900239A CN1900239A CN 200610103614 CN200610103614A CN1900239A CN 1900239 A CN1900239 A CN 1900239A CN 200610103614 CN200610103614 CN 200610103614 CN 200610103614 A CN200610103614 A CN 200610103614A CN 1900239 A CN1900239 A CN 1900239A
- Authority
- CN
- China
- Prior art keywords
- oil
- magnetic field
- reverse magnetic
- boiling fuel
- water
- 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
Links
Landscapes
- Liquid Carbonaceous Fuels (AREA)
- Solid Fuels And Fuel-Associated Substances (AREA)
Abstract
The present invention is the production process and usage of reverse magnetic field boiling fuel oil. The reverse magnetic field boiling fuel oil is prepared with stalk ethanol, biological gasoline and diesel oil, water, stabilizer A, stabilizer B, combustion promoter toluene and methanol, and detonator ethyl nitrate and pental nitrate, and through reaction at certain temperature in some specific chemical apparatus. The reverse magnetic field boiling fuel oil has low cost, no corrosion to metal, no swelling to rubber, and no pollution to atmosphere, soil and water, and may be used in oil burning boiler, internal combustion engine, etc.
Description
Technical field
The present invention is a kind of manufacture method and range of application of reverse magnetic field boiling fuel oil.
Background technology
The energy, environment, agricultural, population and employment are the principal elements that influences global economy, social sustainable development.Along with the continuous growth of world energy sources demand and the minimizing day by day of world petroleum resource, each state is all cutting down the consumption of energy by every possible means and being devoted to the work of fuel substitute and development research new forms of energy, to alleviate the undue dependence to petroleum resources.China through the reform in more than 20 years, exploitation after, economical, societal benefits constantly increase.Oil development occurred and produced seriously lagging behind the consumption growth, the situation that imbalance between supply and demand becomes increasingly conspicuous, for guaranteeing national sustained economic development, China's imported crude oil amount rises significantly, China's imported crude oil in 2004 is broken through 100,000,000 tons of high pointes first up to 12,272 ten thousand tons.Therefore, developing new renewable energy source is a great scientific research task of benefiting the nation and the people.Now, biosynthesizing fuel both domestic and external is a lot, mainly contains: ethanol, methyl alcohol, coalification oil and animal and plant biosynthesizing fuel oil.But methanol fuel oil exists metallic corrosion, rubber item is produced reasons such as swelling, polluted water, and the U.S. and other western countries have made laws and forbidden the fuel oil that contains methyl alcohol.Ethanol fuel oil exists metallic corrosion, outside swell rubber, mainly is to be main raw material with grain, and cost is higher, is unfavorable for commodity market production.The animal and plant biofuel oil mainly exists metallic corrosion, and outside swell rubber, viscosity is big, and is big to mechanical wear, needs to change the part-structure of original equipment, and marketing has certain degree of difficulty.
Summary of the invention
The objective of the invention is does not have corrosion in order to overcome above defective to metal, and rubber is not had swelling, need not change device structure, and raw material is easy to get, and is with low cost, the technology novelty, and environmentally safe is turned waste into wealth, and comprehensive utilization is benefited the nation and the people.For this reason, the spy has developed reverse magnetic field boiling fuel oil.
Content of the present invention is a kind of manufacture method and range of application of reverse magnetic field boiling fuel oil.
Main ingredient of the present invention is:
Straw ethanol: 15-35%, biofuel, gasoline: 20-45%, stablizer A:5-8%, stablizer B:0.3-0.5%, detonator: ethyl nitrate or nitric acid are defended fat 0.1-0.3%, solubility promoter: methyl alcohol 5-8%, toluene 3-8%, water 15-35%.
In special chemical reaction still and backing field stable reaction still, press 75-85 ℃ temperature of reaction and 1300-1500 rev/min speed of response, react finished product after 45-60 minute.
Manufacturing processed of the present invention was divided into for two steps, and one, the main material production process:
1, straw ethanol manufacture method: with cereal straws such as wheat straw bar, straw, leaf, withered grass is raw material.
(1) pulverize: above raw material is cleaned, and rejecting is gone mouldy, and drains the back is ground into the 1-2 cm long with pulverizer expectation;
(2) hydrolysis: clean water basin are put in expectation soaked about 5-7 days, make its hydrolysis, note hydrolysis time length in winter, summer is slightly short;
(3) boiling: the forage after the hydrolysis is packed in the big iron pan, account for pot volumetrical 1/3, adding clear water to pot edge locates, slowly in iron pan, add concentrated nitric acid again, make that the pH value of solution reaches 5 in the pot, build pot cover, heat 105-115 ℃, boiling 60 minutes adds calcium oxide again in pot, make the solution pH value reach 7;
(4) mix song: pull and push open the forage after the boiling out, admix the distiller's yeast of using clear water furnishing pasty state when waiting to be cooled to 50 ℃, distiller's yeast and straw ratio are 1: 100;
(5) fermentation: the grog that will admix distiller's yeast is packed in the fermentation vat, and the material temperature remains on 30-35 ℃, ferments about 5 days, makes the abundant saccharification of grog;
(6) distillation: the grog of the saccharification of will fermenting moves in the still kettle and adds thermal distillation, can get moisture straw ethanol;
(7) dehydration: aqueous straw ethanol is made anhydrous straw ethanol with the lime evaporation.
2, animal and plant dregs of fat system biogasoline, diesel oil method:
(1) raw material and processing: main raw material has herbaceous plant and xylophyta, herbaceous plant oil comprises: vegetable seeds, peanut, soybean, cotton seed, oily certain herbaceous plants with big flowers etc. pressed edible oil the dregs of fat, oil cake,, xylophyta oil comprises: rosin residues such as the oil cake of tung oil tree, rape, wilson dogwood, pine tree etc., shell.Animal grease comprises: grease residue and the swill grease of animals such as pig, ox, sheep.
(2) the grease residue is removed foreign material such as stone after, put into common big iron pan and be heated to about 130 °.The ratio arm bevelling that adds unslaked lime 15 public hands by 50 kilograms of the dregs of fat stirs and does not lump for well.When the dregs of fat congeal into filament, take out be cooled to behind the solid standby.
(3) destructive distillation: the raw material behind the solid is put into the destructive distillation pot, be heated to 100 ℃, reaction is after 5-6 hour, and flowing out has the smell of burning and smell of petrol black viscous liquid, is exactly crude oil.
(4) cracking: in the ratio of 15 kilograms of purified lime of 50 kilograms of crude oil addings, pour in the cracking reaction still, heat to 300-400 ℃, it is exactly raw petroleum that the crude oil decomposes becomes the hydrocarbon class to flow out.
(5) fractionation: raw petroleum is put into the fractionation still, flow out gasoline when temperature arrives 80-150 ℃, flow out kerosene in the time of 150-200 ℃, the thick liquid that remains in pot is a diesel oil.
3, the manufacture method of stablizer A: N.F,USP MANNITOL and oleic acid are put into reactor in 35: 60 ratio and are added 5% catalyzer alkali or acid again and carry out esterification reaction, make stablizer A.
It more than is main raw material manufacturing processed in the reverse magnetic field boiling fuel oil of the present invention.
Two, the cardinal principle that adds entry among the present invention is: 1, the acetate in the alcohol,diluted (or methyl alcohol), the concentration of formic acid, reduce to the corrosion of engine metal with to the dense bloated coefficient of rubber item.2, reduce the viscosity of biofuel, gasoline, strengthen the flowability of oil.3, through after the backing field magnetization, form stable water-in-oil particulate, be combined to the profit molecular gene, oil is external phase, and water is disperse phase, and the boiling point of oil is than water height, molecular gene at first carries out the transition to boiling point and flashes to boiling at the back water particle that is heated, when the pressure in the oil droplet surpassed oil surface tension and pressure, water vapour breaks through the oil film resistance to be blasted oil droplet to form more tiny oil droplet, microexplosion principle that Here it is.Tiny oil droplet after the blast and air be thorough mixing more, and the fluid burning is safer, so reaction, reduced the carbon granule in the flame, improved oily burning degree, under the anoxybiotic condition, carbon granule that produces owing to Pintsch process in the fuel oil can generate CO and H with steam reaction
2, make the fully burning of carbon granule, react as follows:
Three, the backing field equipment principle is: because the effect in terrestrial magnetic field, any on the Northern Hemisphere fluid all is to flow clockwise when flowing naturally, in the Southern Hemisphere then is to flow counterclockwise, produce backing field stable reaction still (patent is newspaper in addition) in order to change the special invention of oil fuel inertial flow in the mill, through multiple authentication, water, oil, pure good stability, reach 9 months stationary phase the longest.
Embodiment
Embodiments of the invention:
Embodiment 1, the manufacturing of reverse magnetic field boiling fuel oil.
Straw ethanol: 15-35%, biological bavin, gasoline: 20-45%, stablizer A:5-8%, stablizer B: thanomin or two alkanolamine 0.3-0.5%, detonator: ethyl nitrate or nitric acid are defended fat 0.1-0.3%, water 15-35%, solubility promoter: toluene 3-8%, methyl alcohol 5-10%.
Make boiling gasoline, boiling diesel oil, boiling boiler combustion oil and boiling kerosene, boiling heavy oil in the chemical reaction still and in the special backing field stable reaction still.
Embodiment 2, and originally boiling fuel diesel is used for burning boiler.
(1) at word boiler PG4, PG16, GPM8 burner.
(2) add 50 kilograms in water, 80 kilograms, 100 kilograms respectively.
(3) water boils and is respectively 8 minutes, 14 minutes, 26 minutes.
Embodiment 3, on Dongfeng Automobile EQ engine.
(1) starting is smooth, and continous-stable catches fire.
(2) engine structure need not be changed and adjustment has related parameter.
(3) the stifled phenomenon of no gas, load-carrying, climbing power are strong.
Embodiment 4, at diesel engine 1105 type eddy cell types.
(1) need not change the engine any structure.
(2) dynamic property is strong, thermo-efficiency height, good economy performance.
(3) smoke intensity is little, pollution is few, and the energy-saving and environmental protection effect is obvious.
Equally direct injection diesel engine there is effect preferably by the different ratios mode.
Claims (6)
1. reverse magnetic field boiling fuel oil, it is characterized in that, by wheat straw, straw, leaf, the withered grass farming, the straw ethanol that forestry depleted cereal straw fiber raw material is made and by moving, the dregs of fat of vegetables oil, pressed the oil cake of edible oil, the bio oil that the oil foot material is made and by N.F,USP MANNITOL in the starch based or dextrin, glucose, oleic acid in trehalose and the fats or glycerine carry out saponification, the stablizer A that makes behind the esterification reaction is under the dissolving of water, by certain temperature of reaction 75-85 ℃, use during reaction: 45-60 minute, speed of response: 1300-1500 rev/min, in special chemical industry equipment reversed magnetization equipment, combine;
Main component and mass range are: straw ethanol: 15-35%, and biological gasoline, diesel oil: 20-45%, stablizer A:5-8%, detonator: ethyl nitrate or nitric acid are defended fat 0.1-0.3%, water: 15-35%, solubility promoter: methyl alcohol 5-10%, toluene 3-8%;
The summation of each component is 100%.
2. reverse magnetic field boiling fuel oil according to claim 1, it is characterized in that, by straw ethanol 25%, biofuel 35%, water 25%, stablizer A5%, solubility promoter methyl alcohol 10%, in chemical industry interlayer reactor, stirred 45 minutes 80 ℃ of temperature, 1300 rev/mins of rotating speeds, flow into then and stablize finished product after 30 minutes in the backing field equipment, can be used as low cheap combustion oil, replace coal, liquefaction vapour, the water oleyl alcohol was not stratified in two months.
3. reverse magnetic field boiling fuel oil according to claim 1, it is characterized in that, straw ethanol 15%, biofuel 45%, toluene 5%, methyl alcohol 10%, stablizer A5%, water 20%, in the chemical reaction still, stirred 60 minutes, temperature control 75-80 ℃, 1500 rev/mins of rotating speeds flow into and stablize finished product after 30 minutes in the backing field equipment, 3-5 month stationary phase is not stratified, can be used as No. 90 cheap gasoline and uses.
4. reverse magnetic field boiling fuel oil according to claim 1, it is characterized in that, straw ethanol 20%, biofuel 45%, stablizer A8%, stablizer B0.5%, solubility promoter methyl alcohol 10%, ignition dope: nitric acid ethanol or nitric acid are defended fat 2%, water 14.5%, in the chemical industry special reactor, stirred 60 minutes, temperature control 75-80 ℃, 1500 rev/mins of rotating speeds enter and stablize finished product after 30 minutes in the backing field equipment, can be used as No. 0 cheap diesel oil and use, 3-6 month stationary phase is not stratified.
5. according to claim 1 or 2 or 3 or 4 described reverse magnetic field boiling fuel oils, it is characterized in that, can produce No. 90, No. 93, No. 97 gasoline and No. 0, negative No. 20 diesel oil respectively in the different mass ratio, mainly be used in gasoline, diesel motor and the various oil-firing boiler.
6. according to claim 1 or 2 or 3 or 4 described reverse magnetic field boiling fuel oils, it is characterized in that the synthesis device of reverse magnetic field boiling fuel oil must be explosion-proof, anti-flaming, rot-resistant chemical reaction still and three anti-backing field stable reaction stills.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200610103614 CN1900239A (en) | 2006-07-25 | 2006-07-25 | Reverse magnetic field boiling fuel oil |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200610103614 CN1900239A (en) | 2006-07-25 | 2006-07-25 | Reverse magnetic field boiling fuel oil |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN1900239A true CN1900239A (en) | 2007-01-24 |
Family
ID=37656229
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 200610103614 Pending CN1900239A (en) | 2006-07-25 | 2006-07-25 | Reverse magnetic field boiling fuel oil |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN1900239A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104357100A (en) * | 2014-10-30 | 2015-02-18 | 黑龙江恒大高新技术有限公司 | High-efficiency clean fuel oil |
-
2006
- 2006-07-25 CN CN 200610103614 patent/CN1900239A/en active Pending
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104357100A (en) * | 2014-10-30 | 2015-02-18 | 黑龙江恒大高新技术有限公司 | High-efficiency clean fuel oil |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| Vasudevan et al. | Liquid fuel from biomass: an overview | |
| Worldwatch Institute | Biofuels for transport: global potential and implications for sustainable energy and agriculture | |
| Demirbas et al. | Biowastes-to-biofuels | |
| Granda et al. | Sustainable liquid biofuels and their environmental impact | |
| Ravikumar et al. | Performance and emission analysis on blends of diesel, restaurant yellow grease and n-pentanol in direct-injection diesel engine | |
| Bajpai | Advances in bioethanol | |
| Capodaglio et al. | Ecofuel feedstocks and their prospects | |
| Bajpai | Developments in bioethanol | |
| Panchuk et al. | Main trends of biofuels production in Ukraine | |
| Houghton-Alico | Alcohol fuels: policies, production, and potential | |
| Yun | Alcohol fuels: current status and future direction | |
| Yadav et al. | Potential utilization of turpentine oil as an alternative fuel | |
| Mathewson | The manual for the home and farm production of alcohol fuel | |
| Sentanuhady et al. | Recent progress on the implementation of renewable biodiesel fuel for automotive and power plants: raw materials perspective | |
| Andrade et al. | Sustainable bioenergy production | |
| Pardilhó et al. | Bioethanol Production from Marine Macroalgae Waste: Optimisation of Thermal acid Hydrolysis | |
| Alhassan et al. | Review of the use of bioethanol as alternative fuel for internal combustion engines | |
| Singh et al. | Biofuel from wastes an economic and environmentally feasible resource | |
| CN1900239A (en) | Reverse magnetic field boiling fuel oil | |
| Pugalendhi et al. | Handbook on Renewable Energy and Green Technology | |
| Dubey et al. | Biomass: sustainable energy solution from agriculture | |
| Sharma et al. | Introduction to lignocellulosic ethanol | |
| Bharathiraja et al. | BIOFUELS: A Promising Alternate for Next Generation Fuels | |
| CN1908127A (en) | Phytol fuel and special engine | |
| Gupta et al. | Biofuels—Future Fuels |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C12 | Rejection of a patent application after its publication | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20070124 |