CN102676250A - Oxygen-rich, liquefied gas - Google Patents
Oxygen-rich, liquefied gas Download PDFInfo
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- CN102676250A CN102676250A CN2011100600651A CN201110060065A CN102676250A CN 102676250 A CN102676250 A CN 102676250A CN 2011100600651 A CN2011100600651 A CN 2011100600651A CN 201110060065 A CN201110060065 A CN 201110060065A CN 102676250 A CN102676250 A CN 102676250A
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Abstract
The invention relates to an organic fuel, and particularly discloses to a rich-oxygen liquefied gas. The fuel is prepared by mixing the following raw materials in percentage by weight: 0.3%-0.45% of ferrocene, 3%-5% of toluene, 3%-4% of essence, 7%-12% of sodium hydroxide, 1.5%-3% of dimethyl ether, 3%-5% of potassium permanganate, 10%-20% of petroleum ether and the balance of pentane. Compared with liquefied petroleum gas, the oxygen-rich, liquefied gas is lower in production cost, is more environment-friendly, has high fuel value, is safe to use and is non-toxic, the existing gas furnace does not need to be reformed, and the rich-oxygen liquefied gas can be used by departments and families using gas fuel.
Description
Technical field
The present invention relates to a kind of organic-fuel, be specifically related to a kind of for oil liquefied gas lower and oxygen-rich liquid gasification environmental protection more of production cost.
Background technology
Oil liquefied gas is also claimed LPG liquefied petroleum gas or liquefied gas, mainly as petrochemical materials, is used for hydrocarbon cracking system ethene or steam and transforms preparing synthetic gas, can be used as industry, civilian, automotive fuel.
Along with the fast development of industry with the product for civilian use, will use oil liquefied gas in a large number, and then cause energy dilemma now, will produce a large amount of waste discharges simultaneously in the Nature, also caused the pollution of environment.
Summary of the invention
In order to address the above problem, the object of the present invention is to provide a kind of for oil liquefied gas lower and oxygen-rich liquid gasification environmental protection more of production cost.
For realizing the foregoing invention purpose, technical scheme that the present invention adopts is following:
A kind of oxygen-rich liquid gasification, this fuel is processed by the raw materials mix of following mass percent:
Diamyl iron 0.3-0.45%, toluene 3-5%, essence 3-4%, sodium hydroxide 7-12%, dme 1.5-3%, potassium permanganate 3-5%, sherwood oil 10-20% and surplus pentane.
As optimum proportion prescription of the present invention, its raw materials quality per-cent is following:
Diamyl iron 0.4%, toluene 4%, essence 3.5%, sodium hydroxide 9.5%, dme 2%, potassium permanganate 4%, sherwood oil 15% and pentane 61.6%.
Each item index MV of products obtained therefrom of filling a prescription according to the present invention data of comparing with oil liquefied gas each item index MV are following:
Can know that by last table contrast oxygen rich fuel gas of the present invention and LPG liquefied petroleum gas compare, burned flame of the present invention is the lower and noresidue of green tasteless, theoretical cigarette amount, so the present invention's environmental protection more; Oxygen rich fuel gas of the present invention adopts the decomposition program to carry out large batch of production, and without smelting product, per ton cost is lower.LPG liquefied petroleum gas goes out product again after exploitation is smelted, also can produce corresponding pollution in the smelting process, and cost exceeds near 50% than the present invention, also will receive the restriction of resource, and oxygen rich fuel gas of the present invention does not receive resource limit, can drop into increasing production.
Oxygen rich fuel gas of the present invention is advanced to be accustomed to comparison test according to the standard of LPG liquefied petroleum gas, and each item index all reaches standard, like following table:
Therefore, the present invention is environmental protection relatively more, and cost is lower.And its fuel value is high, safe in utilization, nontoxic, need not to transform existing gas furnace, and all units with fuel gas, family can use.
Embodiment
To combine the practical implementation method to specify the present invention below, be used for explaining the present invention in schematic enforcement of the present invention and explanation, but not as to qualification of the present invention.
Embodiment 1:
Present embodiment discloses a kind of oxygen-rich liquid gasification, and this fuel is processed by the raw materials mix of following mass percent:
Diamyl iron 0.3%, toluene 3%, essence 3%, sodium hydroxide 7%, dme 1.5%, potassium permanganate 3%, sherwood oil 10% and pentane 72.2%.
At first make base-material, add diamyl iron and mix, diamyl iron is dissolved in water with water; Adding toluene again mixes; Add dme with pentane again and mix, the repeated hydrogenation sodium oxide is synthetic afterwards, adds high violent sour first simultaneously and mixes to stir and make it thorough mixing half a hour and left standstill two hours; Being stored in the basin is exactly finished product oxygen-rich liquid gasification, introduces canned copper bottle by pipeline again.
Starting material require and the effect of starting material in prescription:
1, pentane: be regardless of positive isobutyl, all can use molecular formula C5H12, proportion is below 0.63,36.1 degrees centigrade of boiling points.
2, penta iron: because can not be directly and pentane soluble, the effect after combination be smoke elimination, is that a kind of orange powder thing molecular formula C5H3 also is diene iron.
3, but to be alkane alkali again be a kind of white solid heat release to sodium hydroxide, synthesis type NeOH.
4, dme is a kind of water white transparency compressibility liquid, makes the pentane pressurized.
5, also can add alcohols and not wait water H2O.
Industrial production of the present invention is simple, and the fuel value of product is high, and is safe in utilization, nontoxic, need not to transform existing gas furnace, and all units with fuel gas can use, and huge numbers of families can use, and visible demand is wide, is mainly used in industrial combustion gas.
Oxygen rich fuel gas of the present invention and LPG liquefied petroleum gas compare, and this product is low environmental protection, and the product of low emission, burned flame are green tasteless, and the flame that liquefied gas produces is that redness has flavor.
Oxygen rich fuel gas of the present invention adopts the decomposition program to carry out large batch of production, without smelting product, 1800 yuan of per ton costs.And LPG liquefied petroleum gas goes out product again after exploitation is smelted, and also can produce corresponding pollution in the smelting process, and cost quite exceeds 50% than this product, also will receive the restriction of resource.Oxygen rich fuel gas does not receive resource limit, can drop in the whole world to strengthen and produce.
Embodiment 2:
Present embodiment and the embodiment 1 different raw materials quality per-cents that are, wherein:
Diamyl iron 0.45%, toluene 5%, essence 4%, sodium hydroxide 12%, dme 3%, potassium permanganate 5%, sherwood oil 20% and pentane 50.55%.
Embodiment 3:
Present embodiment and the embodiment 1 different raw materials quality per-cents that are, wherein:
Diamyl iron 0.4%, toluene 4%, essence 3.5%, sodium hydroxide 9.5%, dme 2%, potassium permanganate 4%, sherwood oil 15% and pentane 61.6%.
Raw material of the present invention can get from industrial coal, petrochemical industry waste liquid, waste residue and sub product, agricultural byproducts waste, gets according to above mixed reaction.The present invention is can be for oil liquefied gas, can supply people's use of producing, live, and has practiced thrift the petrochemical industry resource simultaneously, reduces disposal of pollutants, protects and has improved environment, has reduced cost, lets common people afford to use, and has really accomplished to benefit the nation and the people.
More than the technical scheme that the embodiment of the invention provided has been carried out detailed introduction; Used concrete example among this paper the principle and the embodiment of the embodiment of the invention are set forth, the explanation of above embodiment only is applicable to the principle that helps to understand the embodiment of the invention; Simultaneously, for one of ordinary skill in the art, according to the embodiment of the invention, the part that on embodiment and range of application, all can change, in sum, this description should not be construed as limitation of the present invention.
Claims (2)
1. an oxygen-rich liquid gasification is characterized in that, this fuel is processed by the raw materials mix of following mass percent:
Diamyl iron 0.3-0.45%, toluene 3-5%, essence 3-4%, sodium hydroxide 7-12%, dme 1.5-3%, potassium permanganate 3-5%, sherwood oil 10-20% and surplus pentane.
2. oxygen-rich liquid gasification according to claim 1 is characterized in that its raw materials quality per-cent is following:
Diamyl iron 0.4%, toluene 4%, essence 3.5%, sodium hydroxide 9.5%, dme 2%, potassium permanganate 4%, sherwood oil 15% and pentane 61.6%.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011100600651A CN102676250A (en) | 2011-03-14 | 2011-03-14 | Oxygen-rich, liquefied gas |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011100600651A CN102676250A (en) | 2011-03-14 | 2011-03-14 | Oxygen-rich, liquefied gas |
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| CN102676250A true CN102676250A (en) | 2012-09-19 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN2011100600651A Pending CN102676250A (en) | 2011-03-14 | 2011-03-14 | Oxygen-rich, liquefied gas |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103820180A (en) * | 2014-03-21 | 2014-05-28 | 王海涛 | Mixed dimethyl ether gas |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1281031A (en) * | 2000-08-01 | 2001-01-24 | 伍鹏雁 | Synthetic liquefied gas as fuel |
| CN1327035A (en) * | 2000-06-06 | 2001-12-19 | 肖坤 | High energy synthetic liquefied gas |
| CN1339569A (en) * | 2000-08-22 | 2002-03-13 | 赵建国 | High enery synthesized liquefied gas |
| CN101250450A (en) * | 2008-04-11 | 2008-08-27 | 庞英才 | High-energy liquid gas and preparation method thereof |
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2011
- 2011-03-14 CN CN2011100600651A patent/CN102676250A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1327035A (en) * | 2000-06-06 | 2001-12-19 | 肖坤 | High energy synthetic liquefied gas |
| CN1281031A (en) * | 2000-08-01 | 2001-01-24 | 伍鹏雁 | Synthetic liquefied gas as fuel |
| CN1339569A (en) * | 2000-08-22 | 2002-03-13 | 赵建国 | High enery synthesized liquefied gas |
| CN101250450A (en) * | 2008-04-11 | 2008-08-27 | 庞英才 | High-energy liquid gas and preparation method thereof |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103820180A (en) * | 2014-03-21 | 2014-05-28 | 王海涛 | Mixed dimethyl ether gas |
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Application publication date: 20120919 |