CN1316489A - Process for preparing synthetic high-energy liquefied gas - Google Patents
Process for preparing synthetic high-energy liquefied gas Download PDFInfo
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- CN1316489A CN1316489A CN 00114463 CN00114463A CN1316489A CN 1316489 A CN1316489 A CN 1316489A CN 00114463 CN00114463 CN 00114463 CN 00114463 A CN00114463 A CN 00114463A CN 1316489 A CN1316489 A CN 1316489A
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- liquefied gas
- synthetic high
- preparing synthetic
- gas
- energy
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Abstract
A process for preparing synthetic high-energy liquefied gas is disclosed. Said liquefied gas contains the petroleum ether as main fuel and the gasifying agent which may be dry gas, potassium permanganate or bimethyl ether, or alcohol. Its advantages include simple process, low cost, high heat value and high combustion effect.
Description
The present invention relates to a kind of process for preparing synthetic high-energy liquefied gas.
In the domestic fuel technical field, because it relates to the requisite that uses in people's daily life, market outlook are quite wide, always be subjected to each research department, researchist's attention deeply, achievement in research emerges in an endless stream, the domestic fuel product category is various, and having plenty of with the alcohols is the fuel of main raw material; Have plenty of with the oil liquefied gas is the fuel of main raw material; Having plenty of petrochemical industry byproduct condensate oil is main fuel, and its kind is quite a lot of innumerable.These fuel respectively have characteristics, its use has changed traditional fiery mode of using with bavin, grass, coal, the energy of saving time, the home environment cleaning, but exist various shortcoming, Aalcohols fuel is as the methyl alcohol class, before and after the burning, in the burning, volatilization, unburnt gas endanger very big to human body, the nervous cost height of the fuel feedstocks of ethanol and other alcohols; Oil liquefied gas accumulating difficulty; Behind the fuel of condensation oils in the bottle excess oil many or the like, need inflate pressurization during the use that has, what have needs preheating, the meeting that the has carbon deposit of smoldering, using of having is quite dangerous.
The purpose of this invention is to provide a kind of process for preparing synthetic high-energy liquefied gas, system is joined simple, and is easy to use, safety and sanitation, and cost is low, the calorific value height.
The present invention is achieved in that and adds vaporized chemical by a certain percentage in main fuel, and it is formulated to press certain step, and used main fuel is a sherwood oil, and vaporized chemical is potassium permanganate, dry gas or dme, alcohol.
The content umber of liquefied synthetic gas each component of the present invention is respectively:
Sherwood oil 86-94
Dry gas 4-10
Potassium permanganate 2-4
Or in sherwood oil, add
Dme 4-6
Alcohol 2-4
For liquid sherwood oil makes it to become gaseous state by vapourizing unit, enter perfect combustion in the kitchen range at normal temperatures and pressures.Gasifier comprises gasifier and second gasification device.A gasifier is packed in the steel cylinder, and the second gasification device is installed on the kitchen range combustion head and (kitchen range is not done other changes).Gasifier is installed one time: cylinder angle valve with 18 * 1.5 screw tap tapping, is connected with gasifier.The silk notch portion seals with seal strip, must not leak gas.Emulsion tube 500mm, one termination gasifier oil inlet pipe, the other end inserts at the bottom of the steel cylinder, as if 1-2cm, the second gasification device is installed at the bottom of steel cylinder, check the second gasification device before installing, by the water test, check in water whether the second gasification device after inflating leaks gas, and ne-leakage can use, open plate behind the kitchen range, the second gasification device tightly is enclosed within on the combustion head of the kitchen range left side, and copper pipe is by kitchen range combustion head upper edge, and joint adds seal strip with coal gas with the glue flexible pipe, tighten with clamp, can system gas then, with a gasifier angle valve having installed on steel cylinder, can sherwood oil in steel cylinder, add vaporized chemical according to prescription, start air compressor, aerating is closed cylinder angle valve earlier to 5-6kg pressure when pressurization stops in steel cylinder, close the air compressor machine valve of giving vent to anger again, the air compressor peak pressure is no more than 8kg pressure.
Embodiment 1 (weight part)
Sherwood oil 90, dry gas 8, potassium permanganate 2.Its synthetic method as previously mentioned.
Embodiment 2 (weight part)
Sherwood oil 94, dry gas 4, potassium permanganate 2.Its synthetic method is identical with embodiment 1.
Embodiment 3 (weight part)
Sherwood oil 92, dme 5, alcohol 3.Its synthetic method is identical with embodiment 1.
Embodiment 4 (weight part)
Sherwood oil 90, dme 6, alcohol 4.Its synthetic method is identical with embodiment 1.
The present invention compared with prior art has the following advantages and effect: the present invention can use retort, also can Directly produce with the large-tonnage hold-up tank, once can produce several tons or ten tons, firepower is strong, the calorific value height, and calorific value reaches 11800 kilocalories/kg, service time is long, and than oil liquefied gas length about 5 hours, system was joined simple, used safety Convenient, kitchen range, steel cylinder are all general, and be nontoxic, smokeless, pollution-free, and combustion efficiency is good, and production cost is low, suitable Should promote.
Claims (3)
1, a kind of process for preparing synthetic high-energy liquefied gas is made up of main fuel, vaporized chemical, it is characterized in that used main fuel is a sherwood oil, and vaporized chemical is dry gas, potassium permanganate or dme, alcohol.
2, process for preparing synthetic high-energy liquefied gas as claimed in claim 1 is characterized in that, the proportioning of various compositions is in the fuel: sherwood oil 86-94, dry gas 6-10, potassium permanganate 2-4.
3, process for preparing synthetic high-energy liquefied gas as claimed in claim 1 is characterized in that dme 4-6, alcohol 2-4.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 00114463 CN1316489A (en) | 2000-04-04 | 2000-04-04 | Process for preparing synthetic high-energy liquefied gas |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 00114463 CN1316489A (en) | 2000-04-04 | 2000-04-04 | Process for preparing synthetic high-energy liquefied gas |
Publications (1)
Publication Number | Publication Date |
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CN1316489A true CN1316489A (en) | 2001-10-10 |
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Family Applications (1)
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CN 00114463 Pending CN1316489A (en) | 2000-04-04 | 2000-04-04 | Process for preparing synthetic high-energy liquefied gas |
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Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2002081895A1 (en) * | 2001-04-09 | 2002-10-17 | Turner, Geoffrey, Russell | Fuel delivery system |
CN101851538A (en) * | 2010-04-27 | 2010-10-06 | 罗定市升隆科技有限公司 | Combustion promoter for welding-cutting gas and welding-cutting liquid containing the same |
CN101250450B (en) * | 2008-04-11 | 2010-10-13 | 庞英才 | High-energy liquid gas and preparation method thereof |
-
2000
- 2000-04-04 CN CN 00114463 patent/CN1316489A/en active Pending
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2002081895A1 (en) * | 2001-04-09 | 2002-10-17 | Turner, Geoffrey, Russell | Fuel delivery system |
CN101250450B (en) * | 2008-04-11 | 2010-10-13 | 庞英才 | High-energy liquid gas and preparation method thereof |
CN101851538A (en) * | 2010-04-27 | 2010-10-06 | 罗定市升隆科技有限公司 | Combustion promoter for welding-cutting gas and welding-cutting liquid containing the same |
CN101851538B (en) * | 2010-04-27 | 2013-05-01 | 罗定市升隆科技有限公司 | Combustion promoter for welding-cutting gas and welding-cutting liquid containing the same |
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Legal Events
Date | Code | Title | Description |
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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 |