CN1224749A - Synthetic liquid fuel and its production process - Google Patents
Synthetic liquid fuel and its production process Download PDFInfo
- Publication number
- CN1224749A CN1224749A CN 98100282 CN98100282A CN1224749A CN 1224749 A CN1224749 A CN 1224749A CN 98100282 CN98100282 CN 98100282 CN 98100282 A CN98100282 A CN 98100282A CN 1224749 A CN1224749 A CN 1224749A
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- China
- Prior art keywords
- liquid fuel
- retort
- synthetic liquid
- ethanol
- methyl alcohol
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- 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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Abstract
The synthetic liquid fuel is compounded with basic material including methanol and ethanol as well as additives including stearic acid, peroxide of oil and grease, potassium chlorate, zinc peroxide, methyl benzene, methane, cyclohexane, etc. and through mixing and heating to react. The present invention has high heat value and good atomizing and burning effect and can meet the requirement of relevant environment protection standard. It may be used to replace diesel oil and other petroleum product used in power generation, casting, building material and other industrial fields.
Description
The present invention relates to a kind of synthetic liquid fuel and production method thereof, belong to the industrial fuel of alcohols, it is base-material by methyl alcohol, ethanol and is equipped with some additives and makes.
Aalcohols fuel is base-material and the Aalcohols fuel that is equipped with other additive with methyl alcohol, ethanol particularly, existing both at home and abroad a lot of application reports and patent application.But low as industrial fuel ubiquity calorific value, flash-point is low and toxicity is bigger, shortcomings such as cost height.
Purpose of the present invention is exactly that proposing a kind of is the synthetic liquid fuel and the production method thereof of base-material with methyl alcohol, this fuel contains the additive of formulated, and its combustion heat value is higher, and production technique is simple, be suitable for scale operation, and be applied in industrial sectors such as generating, casting, boiler.
The objective of the invention is to finish by following measure:
Each composition weight percent of synthetic liquid fuel is:
Methyl alcohol 70～80%
Ethanol 8～11%
Stearic acid 1～2%
Oxidation grease 12～14%
Potcrate 1～2%
Zinc peroxide 0.01～0.1%
Toluene 0.5～1%
Methane 0.1～0.5%
Hexanaphthene 0.1～0.5%
With ethanol, Potcrate, zinc peroxide, toluene, methane, 6 kinds of raw materials of stearic acid in accordance with regulations proportioning import respectively and mix stirring in the retort, be heated between 55 ℃-65 ℃, about about 30-40 of time minute.The retort that above-mentioned raw materials is equipped with by the proportioning input in the miscible back of thickened oil alicyclic ring hexane heated 10 minutes, 55 ℃～65 ℃ of the interior temperature of the retort of must controlling well at this moment.After the mixture of oxidation grease and hexanaphthene is dissolved in mixtures such as ethanol, again methyl alcohol is joined in the retort by proportioning.React after 20 minutes, remove by filter impurity after, be finished product.
Advantage of the present invention is: synthetic liquid fuel calorific value height, on average can reach after tested more than 10000 kilocalories, and substitute diesel oil as boiler of power plant igniting and combustion-supporting, its cost is low, and complete compliance with environmental protection requirements.In addition, production technique of the present invention is safe and simple.As a kind of efficient, fine synthol, the present invention also can be applied to fields such as building materials, casting and diesel car.Following table is combustion testing result of the present invention:
The project indicator
The light yellow transparent liquid of form
Combustion heat value 12900 card/grams
60 ℃ of burning-points
65 ℃ of flash-points
Kinematic viscosity 2.3MM
2
PH value 6-6.5
SO
2Content 0.8mg/g
Accompanying drawing is production technique figure of the present invention
For an embodiment, each composition weight percent of synthetic liquid fuel is as follows below:
Methyl alcohol 72%
Ethanol 10.5%
Stearic acid 1.5%
Oxidation grease 12%
Potcrate 2%
Zinc peroxide 0.1%
Toluene 0.9%
Methane 0.5%
Hexanaphthene 0.5%
With ethanol, Potcrate, zinc peroxide, toluene, methane, 6 kinds of raw materials of stearic acid in accordance with regulations proportioning import respectively and mix stirring in the retort, be heated to 60 ℃, about about 40 minutes of time.The retort that above-mentioned raw materials is equipped with by the proportioning input in the miscible back of thickened oil alicyclic ring hexane heated 10 minutes, 60 ℃ of the interior temperature of the retort of must controlling well at this moment.After the mixture of oxidation grease and hexanaphthene is dissolved in mixtures such as ethanol, again methyl alcohol is joined in the retort by proportioning.React after 20 minutes, remove by filter impurity after, be finished product.
Claims (2)
1, a kind of synthetic liquid fuel, it is to be base-material with methyl alcohol, and is equipped with that additive makes, and it is characterized in that each composition weight percent of synthetic liquid fuel is:
Methyl alcohol 70～80%
Ethanol 8～11%
Stearic acid 1～2%
Oxidation grease 12～14%
Potcrate 1～2%
Zinc peroxide 0.01～0.1%
Toluene 0.5～1%
Methane 0.1～0.6%
Hexanaphthene 0.1～0.5%
2, a kind of production method of synthetic liquid fuel, it is characterized in that with ethanol, Potcrate, zinc peroxide, toluene, methane, 6 kinds of raw materials of stearic acid in accordance with regulations proportioning import respectively and mix stirring in the retort, be heated between 55 ℃-65 ℃, about about 30-40 of time minute.The retort that above-mentioned raw materials is equipped with by the proportioning input in the miscible back of thickened oil alicyclic ring hexane heated 10 minutes, 55 ℃～65 ℃ of the interior temperature of the retort of must controlling well at this moment.After the mixture of oxidation grease and hexanaphthene is dissolved in mixtures such as ethanol, again methyl alcohol is joined in the retort by proportioning.React after 20 minutes, remove by filter impurity after, be finished product.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 98100282 CN1224749A (en) | 1998-01-25 | 1998-01-25 | Synthetic liquid fuel and its production process |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 98100282 CN1224749A (en) | 1998-01-25 | 1998-01-25 | Synthetic liquid fuel and its production process |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN1224749A true CN1224749A (en) | 1999-08-04 |
Family
ID=5215933
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 98100282 Pending CN1224749A (en) | 1998-01-25 | 1998-01-25 | Synthetic liquid fuel and its production process |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN1224749A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101486938B (en) * | 2009-02-12 | 2013-01-16 | 朱周周 | Catalyst, diesel and alcohol diesel |
| CN108587696A (en) * | 2018-03-24 | 2018-09-28 | 金乐峰 | A kind of environment-friendly type combined diesel oil and preparation method thereof |
-
1998
- 1998-01-25 CN CN 98100282 patent/CN1224749A/en active Pending
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101486938B (en) * | 2009-02-12 | 2013-01-16 | 朱周周 | Catalyst, diesel and alcohol diesel |
| CN108587696A (en) * | 2018-03-24 | 2018-09-28 | 金乐峰 | A kind of environment-friendly type combined diesel oil and preparation method thereof |
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| C06 | Publication | ||
| PB01 | Publication | ||
| C57 | Notification of unclear or unknown address | ||
| DD01 | Delivery of document by public notice |
Addressee: Suo Xianfu Cao Feng Document name: Expiration notice |
|
| C57 | Notification of unclear or unknown address | ||
| DD01 | Delivery of document by public notice |
Addressee: Suo Xianfu Cao Feng Document name: Notice of payment as a notice of withdrawal |
|
| C01 | Deemed withdrawal of patent application (patent law 1993) | ||
| WD01 | Invention patent application deemed withdrawn after publication |