CN1059754A - Hydrolytic hydrogan solid fuel and manufacturing thereof - Google Patents
Hydrolytic hydrogan solid fuel and manufacturing thereof Download PDFInfo
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- CN1059754A CN1059754A CN 90107525 CN90107525A CN1059754A CN 1059754 A CN1059754 A CN 1059754A CN 90107525 CN90107525 CN 90107525 CN 90107525 A CN90107525 A CN 90107525A CN 1059754 A CN1059754 A CN 1059754A
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Abstract
The present invention is a kind of hydrolytic hydrogan solid fuel of compound, can be used for family, tourism and field work, this fuel adopts and adds catalyzer, its composition is a sodium-chlor, SODIUMNITRATE, urea, red phosphorus, sodium bicarbonate can reduce stearic acid usage quantity sixth, cost 1/4th, heat is discharged fully, and hydrolysis hydrogen, increase the fuel heat, thereby the intensity of a fire is prosperous, flare is big, the heat height can be selected fuels with different heat values for use according to energy-conservation principle, the economic utilization energy, manufacture craft of the present invention is simple, is easy to promote.
Description
The present invention relates to a kind of compound solid fuel, particularly relate to a kind of hydrolytic hydrogan solid fuel and manufacturing thereof.
Existing solid fuel removes traditional charcoal, and firewood outside the coal goods, also has some chemosynthesis or chemistry and natural synthetic solid fuel.The former is related to the eubiosis, and resource is not protected, and seriously polluted, influences its use value and range of application; There is pollution problem equally in the latter, and it costs an arm and a leg, and DEVELOPMENT PROSPECT is not good.
The solid fuel of making chemically that occur recent years, though solved the problem of some traditional fuels and chemical fuel existence, because of complex process, investment cost is surprising, causes cost higher, also affects its Application and Development.
The object of the present invention is to provide a kind of raw material abundance, cheap, technology is extremely simple, the method for the production hydrolytic hydrogan solid fuel of less investment.Be civilian and industrial and agricultural production, tourism and field work provide health, and is convenient, inexpensive, resourceful new forms of energy.
Generally with the solid fuel of chemosynthesis, adopt stearic acid as gelifying agent, content reaches 8-15%, thereby following two shortcomings are arranged: 1. cost an arm and a leg, cost is higher: thousand yuan of commercially available stearic acid 5-7 per ton.The per kilogram solid fuel can increase cost 0.5-0.7 unit in 10% stearic acid content, and the 23-40%(that accounts for fuel cost changes with the calorific value cost of material); 2. with regard to stearic characteristic, under certain hour and concentration, stearic acid reaches when solidifying, but burn the later stage, stearic acid concentration retrogradation and extinguishing ahead of time, thereby the calorific value material in the fuel only discharges about 85% of heat.How to solve this difficult problem, the patent of invention of State Patent Office's bulletin is not mentioned the way of head it off at present.
The present invention is by a large amount of practices and measure proof: employing is added catalyzer and can be addressed the aforementioned drawbacks.By adding catalyzer following variation takes place: 1. stearic acid can be reduced to original sixth as the usage quantity of gelifying agent, and cost reduces by 1/4th; 2. stearic coagulation force can increase by six times, and reduces stearic acid dosage, and the burning later stage is unlikely flame-out ahead of time, and heat can discharge fully.With per kilogram fuel calorific value 5137 kilocalories is that example is calculated, and has under the catalyzer of the interpolation condition, and the 770 kilocalorie heats of wherein being prevented can obtain discharging and having utilized.
In addition, according to being determined at combustion high temperature and adding under the situation of catalyzer, the water that per kilogram fuel can also decompose about 100 grams changes into hydrogen, and increases heat 382 kilocalories.In a word, because resolving into the heat of hydrogen acquisition, the Accommodation of interpolation catalyzer and portion water reach the 770-1152 kilocalorie unexpectedly.
Solid fuel of the present invention is solid, two fuel of liquid.When lighting with match, can be by the solid-state liquid state that becomes.Normal temperature was solidified as solid-state again in about 15-17 minute down when extinguishing.Because this specific character helps the performance of firepower, therefore, the intensity of a fire is prosperous, and flare is big, the flame zone yellow.Fuels with different heat values, its flame height can reach 190-300mm.
Now list in table 1 adding catalyst component.
Table 1: add catalyst component (accounting for 4-10%)
Composition | Per-cent (%) |
Sodium-chlor SODIUMNITRATE urea red phosphorus sodium bicarbonate | 1-10 0.5-5 1-5 0.1-0.5 0.5-2 |
Selecting to carry out a series of reforms aspect the interpolation catalyzer, raw material is easy to get, low price, and environmentally safe, with short production cycle, easy to operate, production technique is extremely simple, and therefore, less investment is easy to promote.
Embodiments of the invention: with 100 kilograms of products is example.
Take by weighing 2 kilograms of stearic acid, add 8 kilograms of catalyzer, 39 kilograms of calorific value materials, 51 kilograms in tap water.Then, above raw material is poured into the mediation cylinder together, be incubated 20 minutes in 80 degree stirrings Celsius.Container is injected in the product discharging, normal temperature condensation encapsulation.
The calorific value raw material uses alcohol, ketone, alkane, alkene etc.For the purpose of energy-conservation, can select fuels with different heat values as required.Water and calorific value material can produce the fuel of different calorific values by different proportionings.Fuels with different heat values, its heat can be by 2,500-15,000 kilocalorie/kilogram.The calorific value proportion of raw materials is not less than 36% by weight, be lower than this value light blunt, short during combustion; High mixture ratio can reach 78%.
Claims (3)
1, a kind of hydrolytic hydrogan solid fuel is characterized in that adopting the interpolation catalyzer, and and stearic acid, calorific value material and water mix, be incubated 20 minutes 80 degrees centigrade of stirrings.
2, according to the described solid fuel of claim 1., it is characterized in that adding catalyst content is solid-fuelled 6-10%.Its concrete composition is: sodium-chlor 1-10%, and SODIUMNITRATE 0.5-5%, urea are 1-5%, and red phosphorus is 0.1-0.5%, and sodium bicarbonate is 0.5-2%.
3,, it is characterized in that the calorific value raw material is alcohol, ketone according to the described solid fuel of claim 1., alkane, alkene can be selected fuels with different heat values as required, water and calorific value material can produce the fuel of different calorific values by different proportionings, and the calorific value proportion of raw materials is not less than 36% by weight, is up to 78%.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 90107525 CN1059754A (en) | 1990-09-12 | 1990-09-12 | Hydrolytic hydrogan solid fuel and manufacturing thereof |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 90107525 CN1059754A (en) | 1990-09-12 | 1990-09-12 | Hydrolytic hydrogan solid fuel and manufacturing thereof |
Publications (1)
Publication Number | Publication Date |
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CN1059754A true CN1059754A (en) | 1992-03-25 |
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ID=4880588
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN 90107525 Pending CN1059754A (en) | 1990-09-12 | 1990-09-12 | Hydrolytic hydrogan solid fuel and manufacturing thereof |
Country Status (1)
Country | Link |
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CN (1) | CN1059754A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1053462C (en) * | 1996-12-30 | 2000-06-14 | 年鸣放 | Novel motive power machine fuel and producing method |
-
1990
- 1990-09-12 CN CN 90107525 patent/CN1059754A/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1053462C (en) * | 1996-12-30 | 2000-06-14 | 年鸣放 | Novel motive power machine fuel and producing method |
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