CN1231217A - Herbal catalytic composition and device tobe used for fuel energy saving and pollution control - Google Patents
Herbal catalytic composition and device tobe used for fuel energy saving and pollution control Download PDFInfo
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- CN1231217A CN1231217A CN 98108803 CN98108803A CN1231217A CN 1231217 A CN1231217 A CN 1231217A CN 98108803 CN98108803 CN 98108803 CN 98108803 A CN98108803 A CN 98108803A CN 1231217 A CN1231217 A CN 1231217A
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- catalyst
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L10/00—Use of additives to fuels or fires for particular purposes
- C10L10/02—Use of additives to fuels or fires for particular purposes for reducing smoke development
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Abstract
A herbal catalytic composition for controlling the pollution and saving fuel energy, comprising from about 35-45% of Aeyle marmelos, from about 55-65% of Ocimum basilicum where said constituents are soaked in water for the brewing and are grounded with the fungal growth, the said compositions is boiled followed by the evaporation of 3-5% of the said composition, water is added to said composition during heating, the said composition is cooled at the ambient temperature to make the said catalytic composition in concentration form, said catalytic composition is diluted before using.
Description
The present invention relates to useful herbal catalytic composition in fuel saving and control pollution course, nitrogen oxide is converted into nitrogen in catalysed promoted reaction, so theme of the present invention relates to the composition of removing or eliminate the catalyst of nitrogen oxide from belong to public utilities boiler that material acts as a fuel and converter with hydrocarbon in the fuel gas stream that can be used for producing.
The technical staff who pollutes the control field is familiar with many catalyst of having developed that are used for directly reducing fuel gas stream nitrogen.There are several such catalyst can be from commercial acquisition.The common trait of these catalyst is to be used to reduce nitrogen oxide.
One of major defect that exists in converter and the boiler is the root problem in the combustion process, and promptly the each several part in the combustion chamber all needs a large amount of air to guarantee completing combustion.Lack of air will cause the generation of imperfect combustion and unburnt carbon, show as over-emitting black exhaust.Yet, use excess air may and remove the heat that does not need as sensible heat again and cause the poor efficiency operation because of the airborne flame of excess coolant.In this case, not only contain free carbon but also contain fuel gas in the waste gas, thereby cause potential thermal losses.
The second, so the cigarette of discharging forms one deck at the top of converter/boiler.
The technical staff who pollutes the control field is familiar with many catalyst of having developed that are used for directly reducing fuel gas stream nitrogen.There are several such catalyst can be from commercial acquisition.The common trait of these catalyst is to be used to reduce nitrogen oxide.
The functional characteristic situation of alloy production is at first to add metal, when it precipitates, is that benchmark adds other metals and chemical substance with synthetic product then.Between melting stage, the pure oxygen in the converter is cut to accelerate fusion processes by very big pressure by electrical resistance welding tube.
For this operation, will gather considerable liquid oxygen according to the usefulness of converter.
In present converter, the cutting operation of oxygen is pure manual, because the welded pipe in the converter is manual the introducing, up to the fusing point of sending the metal in the converter to.Therefore, because high temperature and insufferable light and heat, can not more approaching hot converter with manpower.Cutting operation always interrupts and discontinuous carrying out, and that this is the Rapid Combination thing of alloy is needed in when fusing.Because such fusing time increases and owing to discontinuous intermittently operated, the gained alloy can not reach the technical specification of the alloy cpd of the correct mixing that needs.
In steel and petro chemical industry, when heating in popular industry, the dinitrogen in the atmosphere is dissociated into its atomic form and easily absorbs and reduces its formability in the steel of heating.This makes it can not be used for the application of the high ductility of needs.In order to produce steel, can further press forging on mould, nitrogen concentration must be reduced to about 30-50PPM.
It is found that, in the steelmaking process of routine, during initial fusing in steel absorbed a large amount of nitrogen, when oxygen being fed when being reacted into carbon in the liquid steel, nitrogen concentration has reduced.Particularly the carbon monoxide that forms in this course of reaction has been finished the thorough cleaning of nitrogen.The existence that covers the foam-like slag on the molten metal has reduced the chance that absorbs more nitrogen.Carbon dioxide during this foam steel is bathed forms minute bubbles and produces in the steel embryo, its density is with approximate at the foam of the top of soda formation.
The greatest problem that faces in the existing industry is energy waste and metallurgical loss.Another ubiquitous subject matter is to pollute.
Similarly, compressed petroleum gas (LPG) is each family the most frequently used and requisite small stores that all will use almost.
We have found that: the ratio of combustion solid or the fluid combustion of combustion gas (industrial/family expenses) are controlled easily, because can control the mixing of fuel and combustion air better.With regard to reach the easy degree of completing combustion with excessive slightly air, under the situation of LPG, mainly the combustion gas of being made up of hydrocarbon is not so good as to contain substantially the admixture of gas of hydrogen and CO part a little.
If the ratio of the fuel gas that the mixture of fuel gas contains is very little or too greatly, it can not be lighted, and can not burn.But this does not also mean that this gas can not the oxidation by this mixture of heating.
The canned LPG that family uses is under the quite low pressure.The largest portion of the LPG that produces is to be used for central heating system, secondly is the raw material as chemical plant.
In order to overcome the shortcoming that is present in the main system, the present invention has made the CO discharge capacity sharply reduce, and has found a kind of catalyst of handling the problems referred to above.
The object of the present invention is to provide a kind of catalyst composition.
We have also found a kind of catalyst of catalyst combustion reaction, in order that the formation of minimizing cigarette and carbon when using LPG in industry and home appliances.
In steel industry, the invention enables and saved fuel, by the fusing time cycle has been shortened 20%, and finally make the fuel losing quantity reduce 20%.This also makes has removed oxygen from system.
The most important purpose of the present invention is a fuel saving, by the fusing cycle is shortened 20%, thereby finally saves electric losing quantity 20%.
Electric arc furnaces mainly is to be used to melt down scrap metal and to add other metals and chemical substance again to produce alloy.By adding catalyst, just can remove the adition process of oxygen in the fusion process.Because the catalyst in the stove is to be used on the auxiliary devices that adds catalyst and to add by designing and make at the load capacity of stove, has therefore also eliminated hand labour.
By add catalyst in stove, equipment passes through the operation of air without any interruption.
Catalyst quickens fusing, also makes the temperature in the stove remain on all metals and the technical standard required temperature of chemical substance mixing to be attached to highest ranking and to need that generates alloy.
The objective of the invention is, by using catalyst, system can not be present in cigarette ash or slag or the obstruction of other particulate matters in the air-flow.
Another free-revving engine of the present invention is: the use of system of the present invention is the system that does not have pollution fully, because catalyst is biologic fully.
The shelf life of Zhi Bei catalyst is more than 1 year, without any polluting or conk like this.
Be used for obtained natural herb plant that composition makes catalyst from wooden tangerine belong to and basil choose.Gather described natural product herbaceous plant and process.Win the blade of described natural materials and it was soaked in the water brew two days.Immersion makes fungi grow on blade.After fungi grows, will grind with the blade mixture of fungi with conventional method, making it become granular size is that the 300-400 purpose is evenly stuck with paste.After uniformly catalyst composition is made, at first be heated and be put in the unlimited oxidation container, boiling 20-40 minute under the boiling temperature in atmosphere then.Mixture is evaporated to the 3-4% of total amount.The evaporation back adds the water more than 25% in this mixture.Again this catalyst composition heating a period of time.The heating back is this mixture cool to room temperature.Cooling concentration this catalyst composition.
When composition is condensed to one, use after in prepared catalyst composition concentrate, adding entry.The water yield that adds should be 10 times of catalyst composition concentrate, and the ratio that concentrates draft catalyst composition and water is 1: 10.In described catalyst, two kinds of plants belong to wooden tangerine: Ocimum is 40: 60 ratio combination.
The present invention relates to be used to control the draft catalyst composition of pollution and fuel saving, it comprises:
The wooden tangerine of about 35-45%
The sweet basil of about 55-65% wherein be described component be soaked in carry out in the water brew and with the growth fungi grind, after boiling said composition, it is evaporated to the 3-5% of total amount, in said composition, add entry in the heating process, the cooling said composition obtains the conc forms of this catalyst composition to room temperature, before the use this catalyst composition is diluted.
Fig. 1 is the flow schematic diagram of the equipment of boiler and coverter pig fuel saving.
Fig. 2 is the flow schematic diagram of electric arc furnaces with fuel saving equipment.
Fig. 3 is the flow schematic diagram of steel industry with fuel saving equipment.
Fig. 4 is the flow schematic diagram of petro chemical industry with fuel saving equipment.
Fig. 5 is the flow schematic diagram of LPG with fuel saving equipment.
Fig. 1 relates to boiler and converter, has wherein filled the catalyst that is up to 5-12% in the catalyst stores device (1).This catalyst stores device (1) has an inlet (1a) and an outlet (1b).The air that can obtain from air delivery pipe (2) sucks by inlet (1a) part of described holder.Air in containing the catalyst chamber of catalyst, circulate and through outlet (1b) enter in the described air delivery pipe (2) and boiler in the air that exists mix.There is a supporting container (3) to link to each other so that keep the amount of the catalyst composition of needs in the described equipment with the major part of the holder that contains catalyst.Holder is filled into the 1/3-1/4 capacity of described catalyst composition.
Fig. 2 relates to electric arc furnaces, has wherein filled the catalyst that is up to 5-12% in the catalyst stores device (1).This catalyst stores device (1) has an inlet (1a) and an outlet (1b).Air in the catalyst chamber is blown into by inlet (1a) from air blast (2).Air circulates by catalyst chamber, passes to the electrode group of electric arc furnaces (3) then through outlet (1b).Supporting container (4) links to each other with the major part of the holder that contains catalyst so that keep the catalyst composition of requirement in the described equipment.Holder is filled into the 1/3-1/4 capacity of described catalyst composition.
Fig. 3 and 4 relates to steel and petro chemical industry, has wherein filled the catalyst that is up to 5-12% in the catalyst stores device (1).This catalyst stores device (1) has a pair of inlet (2) and (2a) and a pair of outlet (3) and (3b).Air sucks by inlet (2) with (2a) from air delivery pipe (4), by the catalyst chamber circulation, and then through exporting (3) and (3a) rotating back into described air delivery pipe (4).Major part is made up of two inlets and two outlets.The supporting container (5) that has an inlet and an outlet links to each other with major part so that keep the amount of needs in the described catalyst stores device.Air in the air delivery pipe is blown into from catalyst stores device (1), and catalyst is filled into 5-12%.
Fig. 5 relates to LPG, and wherein catalyst stores device (1) has an inlet (1a) and an outlet (1b).Air in the catalyst chamber is blown into by inlet (1a) from air delivery pipe (2).Air circulates by catalyst chamber, rotates back into air delivery pipe (2) through outlet (1b) then.Supporting container (3) links to each other with the major part of the holder that contains catalyst so that keep the catalyst composition of requirement in the described equipment.Holder is filled into the 1/3-1/4 capacity of described catalyst composition.
The objective of the invention is,, system can not stopped up by cigarette ash or slag or other particulate matters that is present in the air-flow by using catalyst.Therefore the present invention is useful, because the CO discharge rate is reduced to minimum, the fuel maximum combustion does not have bird nest in boiler and converter.
Under the situation of electric arc furnaces, because eliminated the adition process of oxygen in the fusion process, the present invention is favourable.Because catalyst joins in the stove, therefore also eliminated hand labour.It has shortened 20% with the fusing time cycle, has finally saved electric losing quantity 20%.It has been avoided the oxygen cutting fully and has eliminated fully and cut required foundation structure.This has also been avoided labourer in the work that is not suitable for carrying out in the manual environment.
The present invention is favourable in steel industry, be because eliminated the nitrogen of the main cause that causes scaling loss, and catalyst composition of the present invention is used as the protection thing in combustion process.Except these, also can eliminate the foam material that causes by carbon dioxide, fuel maximum combustion, non-scaling.It is minimum that the present invention can reduce to the metal loss that causes owing to slag and fouling.
The shelf life that the herbal catalyst tool of preparation like this is above one year.The present invention is 100% vegetable composition, does not wherein use synthetic chemical or even anticorrisive agent.The component of the present composition itself is as anticorrisive agent.Catalyst of the present invention be ecological pleasantly with biodegradable.Because all raw materials all are spontaneous growths, and aboundresources, so it is very economical.
Claims (15)
1. one kind is used to control and pollutes and the herbal catalytic composition of fuel saving, and it comprises:
The wooden tangerine of about 35-45%
The sweet basil of about 55-65% wherein be with described component be soaked in carry out in the water brew and with the growth fungi grind, again said composition is boiled, evaporate the 3-5% of said composition then to total amount, in said composition, add entry in the heating process, its cool to room temperature is obtained the conc forms of this catalyst composition, before using this catalyst composition is diluted.
2. it is the 300-400 order that plant catalyst composition as claimed in claim 1, wherein said composition are ground to granular size.
3. plant catalyst composition as claimed in claim 1, wherein said concentrated catalyst composition are with catalyst composition: water is that 1: 10 ratio adds entry and dilutes.
4. the preparation method of plant catalyst composition, component wherein comprises the wooden tangerine of about 35-45% and the sweet basil of 55-65%, they are soaked in water carried out brew in 2-3 days, fungi is grown on described component, then described component is ground and form even pasty state, should evenly stick with paste and be heated to boiling temperature maintenance 20-40 minute, again it is evaporated to the 3-4% of described total composition, ratio with 25% adds water in said composition, heating makes the concentrate of catalyst composition again.
5. one kind is used for the control pollution of boiler and converter, electric arc furnaces, steel and petro chemical industry and LPG and the equipment of fuel saving, wherein the catalyst stores device is the double container that has an inlet and an outlet, and is equipped with and makes the catalyst height remain on 1/3 device of described composition volume.
6. the control pollution of boiler and converter and the equipment of fuel saving of being used for as claimed in claim 5, wherein the inlet of catalyst stores device is connected to air delivery pipe so that air flows to the described holder in carrier pipe.
7. the control pollution of boiler and converter and the equipment of fuel saving of being used for as claimed in claim 5, wherein the outlet of catalyst stores device is connected to air delivery pipe, and air is turned back to the same air delivery pipe after the circulation of catalyst stores device.
8. the control pollution of boiler and converter and the equipment of fuel saving of being used for as claimed in claim 5, the height of wherein said carbon monoxide-olefin polymeric is maintained at about the level into described holder 1/3.
9. the equipment of control pollution as claimed in claim 5 and fuel saving, it is used for boiler and converter, and wherein the height of the catalyst that contains in described holder is kept by supporting container.
10. the control pollution of electric arc furnaces and the equipment of fuel saving of being used for as claimed in claim 5, wherein the inlet of catalyst stores device links to each other with the air delivery pipe of air blast, so that air flows into described holder from air delivery pipe.
11. the equipment of control pollution as claimed in claim 5 and fuel saving, it is used for electric arc furnaces, and wherein the outlet of catalyst stores device links to each other with the electrode group of electric arc furnaces, so that air passes to electric arc furnaces after the circulation of catalyst stores device.
12. the equipment of control pollution as claimed in claim 5 and fuel saving, it is used for steel and petro chemical industry, and wherein the inlet of catalyst stores device links to each other with air delivery pipe, so that air flows into described holder from air delivery pipe.
13. the equipment of control pollution as claimed in claim 5 and fuel saving, it is used for steel and petro chemical industry, and wherein the outlet of catalyst stores device links to each other with air delivery pipe, so that air turns back to the same air delivery pipe from the circulation of catalyst stores device.
14. the equipment of control pollution as claimed in claim 5 and fuel saving, it is used for LPG, and wherein the population of catalyst stores device links to each other with air delivery pipe, so that air flows into described holder from air delivery pipe.
15. the equipment of control pollution as claimed in claim 5 and fuel saving, it is used for LPG, and wherein the outlet of catalyst stores device links to each other with air delivery pipe, so that air turns back to the air delivery pipe after the circulation of catalyst stores device again.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 98108803 CN1231217A (en) | 1998-04-04 | 1998-04-04 | Herbal catalytic composition and device tobe used for fuel energy saving and pollution control |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 98108803 CN1231217A (en) | 1998-04-04 | 1998-04-04 | Herbal catalytic composition and device tobe used for fuel energy saving and pollution control |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN1231217A true CN1231217A (en) | 1999-10-13 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 98108803 Pending CN1231217A (en) | 1998-04-04 | 1998-04-04 | Herbal catalytic composition and device tobe used for fuel energy saving and pollution control |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN1231217A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2001072931A1 (en) * | 2000-03-30 | 2001-10-04 | Biool | Hydrocarbon grade fuel from biomass mixture |
-
1998
- 1998-04-04 CN CN 98108803 patent/CN1231217A/en active Pending
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2001072931A1 (en) * | 2000-03-30 | 2001-10-04 | Biool | Hydrocarbon grade fuel from biomass mixture |
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| C06 | Publication | ||
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| C02 | Deemed withdrawal of patent application after publication (patent law 2001) | ||
| WD01 | Invention patent application deemed withdrawn after publication |