CN1327035A - High energy synthetic liquefied gas - Google Patents
High energy synthetic liquefied gas Download PDFInfo
- Publication number
- CN1327035A CN1327035A CN 00109082 CN00109082A CN1327035A CN 1327035 A CN1327035 A CN 1327035A CN 00109082 CN00109082 CN 00109082 CN 00109082 A CN00109082 A CN 00109082A CN 1327035 A CN1327035 A CN 1327035A
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- China
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- weight part
- liquefied gas
- high energy
- essence
- dme
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Abstract
The high energy synethetic liquefied gas is compounded with pentane in 100 (in weight portions, the same as below), dimethyl ester 0.25-0.45, ferrocene 0.005-0.015, toluene 0.02-0.05, sodium hydroxide 0.07-0.12 and essence or mercaptan 0.03-0.05. The present invention has easy production process, low cost, no pollution and high combustion value and may be used widely in countryside.
Description
The present invention relates to a kind of high energy synthetic liquefied gas, belong to the fuel industry technical field.
Existing industry or civilian oil liquefied gas, be that the gas that produces in petroleum refining process is made through pressurized liquefied, will store in high pressure gas holder, reduce to a normal atmosphere through reducing valve and use, not only thermo-efficiency is low, and easy leakage of high pressure gas holder sets off an explosion, presence of fire is used high pressure gas holder to store and has been improved cost, and the gas that leaks out is toxic to human body and animals and plants, atmosphere is produced pollution, destroy the eubiosis.
The objective of the invention is weak point, adopt industrial chemicals and additive to be mixed with a kind of thermo-efficiency height, high energy synthetic liquefied gas easy to use, safe and reliable at above-mentioned oil liquefied gas.
Of the present invention theing contents are as follows:
1. used starting material title and purity requirement:
1, pentane technical pure
2, dimethylether industrial is pure
3, ferrocene technical pure
4, toluene technical pure
5, sodium hydroxide technical pure
6, essence technical pure
7, mercaptan technical pure
2. cooperate proportional range:
Pentane 100 (weight part)
Dme 0.25-0.45 (weight part)
Ferrocene 0.005-0.015 (weight part)
Toluene 0.02-0.05 (weight part)
Sodium hydroxide 0.07-0.12 (weight part)
Essence or mercaptan 0.03-0.05 (weight part)
Compound method is as follows:
Take by weighing raw material by above-mentioned weight proportion scope, normal temperature and pressure preparation in the retort of belt stirrer, add pentane earlier, ferrocene with after the toluene dissolving, is added retort, add sodium hydroxide, essence again, add dme at last, stirred 3-5 minutes, left standstill 15-20 minutes, can is advanced in the normal pressure steel cylinder can be sold to the user.
The best ratio range of said ratio:
Pentane 100 (weight part)
Dme 0.3-0.4 (weight part)
Ferrocene 0.008-0.012 (weight part)
Toluene 0.02-0.04 (weight part)
Sodium hydroxide 0.09-0.11 (weight part)
Essence 0.04-0.05 (weight part)
The best proportioning of said ratio scope is:
Pentane 100 (weight part, as follows)
Dme 0.3 (weight part) (summer)
Ferrocene 0.01 (weight part)
Toluene 0.03 (weight part)
Sodium hydroxide 0.1 (weight part)
Essence 0.05 (weight part)
In the above-mentioned prescription, used for dimethyl ether 0.4 (weight part) in the winter time, essence can replace with the mercaptan of same ratio.
The invention has the advantages that manufacturing process is simple, production safety, cost is low, cheap, each household resident every month consumes 1.50 yuan of 13kg per kilogram costs, and promptly every month fuel cost is the highest to be no more than 20 yuan, only be half of market liquefied gas price, use product of the present invention to reduce to oil coal tangerine bar and wood usage amount, nontoxic during burning, pollution-free, no stink, no flue dust, no carbon distribution, inflammable, non-explosive, have safety, health, characteristics such as easy to use, calorific value is 98.3mj/m
3, firepower is violent, and flame temperature uses common steel cylinder to get final product can more than 1000 ℃, simple to operate during use, comprehensive cost is lower than oil liquefied gas, can solve and improve the problem of rural area short bunker effectively, and environment purification, save energy has obvious social and economic benefit.
Embodiment:
With the retort of a belt stirrer, add following raw material, 1000 kilograms of pentanes, with 0.1 kilogram of 0.3 kilogram of toluene dissolving ferrocene, add in the jar 1 kilogram of repeated hydrogenation sodium oxide, 0.5 kilogram in essence (or mercaptan) adds 3 kilograms of dme at last, starts agitator and stirs 5 minutes, leave standstill and got final product can in 20 minutes, if the rural area small-scale production, personnel 5 people, 4000 yuan of facility investment, 5000 yuan of current assetss, factory building 100m
2, can go into operation, can go into operation this month, makes a profit ten thousand yuan.Workman with junior middle school's educational level can receive training and produce.
Claims (6)
1, a kind of high energy synthetic liquefied gas is characterized in that: its weight proportion scope is:
Pentane 100 (weight part)
Dme 0.25-0.45 (weight part)
Ferrocene 0.005-0.015 (weight part)
Toluene 0.02-0.05 (weight part)
Sodium hydroxide 0.07-0.12 (weight part)
Essence or mercaptan 0.03-0.05 (weight part)
2, high energy synthetic liquefied gas according to claim 1 is characterized in that above-mentioned weight proportion preferred range is:
Pentane 100 (weight part)
Dme 0.3-0.4 (weight part)
Ferrocene 0.008-0.012 (weight part)
Toluene 0.02-0.04 (weight part)
Sodium hydroxide 0.09-0.11 (weight part)
Essence 0.04-0.05 (weight part)
3, high energy synthetic liquefied gas according to claim 1 is characterized in that above-mentioned weight proportion the best is:
Pentane 100 (weight part)
Dme 0.3 (weight part) (summer)
Ferrocene 0.01 (weight part)
Toluene 0.03 (weight part)
Sodium hydroxide 0.1 (weight part)
Essence 0.05 (weight part)
4, high energy synthetic liquefied gas according to claim 3 is characterized in that: the consumption of dme is used 0.4 (weight part) in the winter time.
5, high energy synthetic liquefied gas according to claim 4 is characterized in that: essence wherein can replace with the mercaptan of same ratio.
6, according to the described high energy synthetic liquefied gas of claim 1-5, it is characterized in that: the compound method of described liquefied gas is:
Take by weighing raw material by aforesaid right requirement 1-5 weight proportion scopes, normal temperature and pressure preparation in the retort of belt stirrer, the steps include: to take by weighing raw material by the weight proportion scope of claim 1-5, add pentane earlier, add again, add sodium hydroxide, essence (or mercaptan) successively with toluene dissolved ferrocene, add dme at last, stirred 3-5 minutes, left standstill 15-20 minutes, the steel cylinder (normal pressure is airtight) of can packing into.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 00109082 CN1327035A (en) | 2000-06-06 | 2000-06-06 | High energy synthetic liquefied gas |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 00109082 CN1327035A (en) | 2000-06-06 | 2000-06-06 | High energy synthetic liquefied gas |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN1327035A true CN1327035A (en) | 2001-12-19 |
Family
ID=4579406
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 00109082 Pending CN1327035A (en) | 2000-06-06 | 2000-06-06 | High energy synthetic liquefied gas |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN1327035A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101250450B (en) * | 2008-04-11 | 2010-10-13 | 庞英才 | High-energy liquid gas and preparation method thereof |
| CN102676250A (en) * | 2011-03-14 | 2012-09-19 | 云南牛选科技有限公司 | Oxygen-rich, liquefied gas |
-
2000
- 2000-06-06 CN CN 00109082 patent/CN1327035A/en active Pending
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101250450B (en) * | 2008-04-11 | 2010-10-13 | 庞英才 | High-energy liquid gas and preparation method thereof |
| CN102676250A (en) * | 2011-03-14 | 2012-09-19 | 云南牛选科技有限公司 | Oxygen-rich, liquefied gas |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C06 | Publication | ||
| PB01 | Publication | ||
| C02 | Deemed withdrawal of patent application after publication (patent law 2001) | ||
| WD01 | Invention patent application deemed withdrawn after publication |