CN205714420U - Utilize methanol aqueous solution as the burner of fuel - Google Patents
Utilize methanol aqueous solution as the burner of fuel Download PDFInfo
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- CN205714420U CN205714420U CN201620337815.3U CN201620337815U CN205714420U CN 205714420 U CN205714420 U CN 205714420U CN 201620337815 U CN201620337815 U CN 201620337815U CN 205714420 U CN205714420 U CN 205714420U
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- aqueous solution
- evaporation device
- methanol aqueous
- fuel
- combustion mechanism
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02T—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
- Y02T10/00—Road transport of goods or passengers
- Y02T10/10—Internal combustion engine [ICE] based vehicles
- Y02T10/12—Improving ICE efficiencies
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02T—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
- Y02T10/00—Road transport of goods or passengers
- Y02T10/10—Internal combustion engine [ICE] based vehicles
- Y02T10/30—Use of alternative fuels, e.g. biofuels
Abstract
A kind of utilizing methanol aqueous solution as the burner of fuel, including evaporation device and combustion mechanism, the venthole of evaporation device is connected with the fuel air pipe of combustion mechanism by air shooter, and evaporation device is arranged on the exhaust position of combustion mechanism；During combustion mechanism work, heating the heat that exhaust position produces as heating source to the methanol aqueous solution in evaporation device, making methanol aqueous solution become methanol steam, methanol steam is transported in combustion mechanism burning by air shooter.The utility model is owing to have employed evaporation device and combustion mechanism, methanol aqueous solution in evaporation device is heated by heating source, methanol aqueous solution is made to become methanol steam and be transported in combustion mechanism burning, during burning, methanol steam is as main fuel, and can generate carbon dioxide and water after combustion；There is simple in construction, pollution-free, zero-emission, completely burning, the saving energy and reduce the advantages such as energy loss.
Description
Technical field
The utility model relates to clean energy technology field, especially relates to a kind of utilize methanol aqueous solution as the burner of fuel.
Background technology
The development of auto industry is significant at global economic development, but the large quantity of exhaust gas that automobile is discharged has resulted in serious pollution, endangers the living environment of our mankind.The burning of in-engine fuel oil is the source of automobile power, is also the main place that automobile produces pollutant.On the one hand, the waste gas that engine combustion is discharged has taken away a part of heat, causes the loss of energy, and on the other hand, the waste gas that engine combustion is discharged causes the pollution of environment.
The oil sent by the fuel tank of vehicle and the air of inlet manifold input, upon mixing ignition, blast in entrance engine, and the piston work done in drive engine.There are about in combustion 1/3 fuel unburned complete, and discharged by blast pipe with waste gas, make exhaust emission degree higher, affect air quality, be harmful to environmental protection.In order to make fuel be burnt completely during burning, or burnt to greatest extent, reduced the loss of energy, a kind of engine hydrogenation plant of people's utility model.This engine hydrogenation plant is to utilize engine heat to start methyl alcohol reformer, and methanol aqueous solution is made hydrogen by methyl alcohol reformer, then passes through the combustion-supporting to improve efficiency of combustion in engine for the fuel oil of hydrogen.Although this engine hydrogenation plant achieves certain effect in terms of improving efficiency of combustion, but its structure is complicated, need methanol aqueous solution is made hydrogen, and hydrogen is as auxiliary fuel, main fuel or fuel oil, still can there is a part of fuel oil during burning imperfect combustion, the waste gas discharged after therefore burning still pollutes the environment.
Utility model content
In order to overcome the problems referred to above, the utility model to society provide a kind of simple in construction, pollution-free, zero-emission and can burn completely utilize methanol aqueous solution as the burner of fuel.
A kind of technical scheme of the present utility model is: provides and a kind of utilizes methanol aqueous solution as the burner of fuel, including evaporation device and combustion mechanism, the venthole of described evaporation device is connected with the fuel air pipe of described combustion mechanism by air shooter, and described evaporation device is arranged on the exhaust position of described combustion mechanism；During the work of described combustion mechanism, the heat producing described exhaust position heats as heating source to the methanol aqueous solution in described evaporation device, making described methanol aqueous solution become methanol steam, described methanol steam is transported in described combustion mechanism burning by described air shooter.
As to improvement of the present utility model, also including methyl alcohol water storage apparatus, described methyl alcohol water storage apparatus is connected with the inlet opening of described evaporation device by connecting tube.
As to improvement of the present utility model, the blast pipe of described combustion mechanism is partially or completely surrounded by described evaporation device, and described evaporation device and described blast pipe are in laminating shape, in order to absorb the heat lift temperature of waste gas.
As to improvement of the present utility model, described evaporation device is arranged in the blast pipe of described combustion mechanism, in order to absorb the heat lift temperature of the waste gas in described blast pipe.
As to improvement of the present utility model, also including the catalysis material containing copper, described catalysis material is arranged in described evaporation device, and contacts with the described methanol aqueous solution in described evaporation device.
As to improvement of the present utility model, described catalysis material is pure copper material or Cu alloy material.
As to improvement of the present utility model, described Cu alloy material is beallon material.
As to improvement of the present utility model, described combustion mechanism is boiler or internal combustion engine.
The utility model is owing to have employed evaporation device and combustion mechanism, methanol aqueous solution in evaporation device is heated by heating source, methanol aqueous solution is made to become methanol steam, then methanol steam is transported in combustion mechanism burning, during burning, methanol steam is as main fuel, and can generate carbon dioxide and water after combustion；Heating source uses the heat of the blast pipe in combustion mechanism, so can reduce energy loss, maximally utilise the heat of waste gas in blast pipe；Catalysis material can also be used in evaporation device, catalysis material is during heating, methanol aqueous solution can be made to produce hydrogen and carbon monoxide, so advantageously in the burning completely of methanol steam, release energy to greatest extent, there is simple in construction, pollution-free, zero-emission, completely burning, the saving energy and reduce the advantages such as energy loss.
Brief description
Fig. 1 is the planar structure schematic diagram of a kind of embodiment of the present utility model.
Fig. 2 is the planar structure schematic diagram of another kind of embodiment of the present utility model.
Wherein: 1. combustion mechanism；11. blast pipes；2. evaporation device；3. methyl alcohol water storage apparatus；4. connecting tube；5. air shooter.
Detailed description of the invention
In of the present utility model description, it will be appreciated that, in term, the orientation of the instruction such as " " center ", " on ", D score, "front", "rear", "left", "right" or position relationship are for based on orientation shown in the drawings or position relationship; be for only for ease of description the utility model and simplifying and describe; rather than instruction or hint indication device or element must have specific orientation, with specific azimuth configuration and operation, therefore it is not intended that to restriction of the present utility model.Additionally, term " first ", " second " are only used for describing purpose, and it is not intended that instruction or hint relative importance.
In of the present utility model description, it should be noted that unless otherwise clearly defined and limited, term " is installed ", " connection ", " being connected " should be interpreted broadly, for example, it may be fixing connection, it is also possible to it is to dismantle connection, or be integrally connected；Can be to be mechanically connected, it is also possible to be electrical connection；Can be to be joined directly together, it is also possible to be to be indirectly connected to by intermediary, can be the connection of two element internals.For the ordinary skill in the art, above-mentioned term can be understood at concrete meaning of the present utility model with concrete condition.
The utility model provides and a kind of utilizes methanol aqueous solution as the combustion method of fuel, methanol aqueous solution is joined in evaporation device, the described methanol aqueous solution joining in described evaporation device is heated by heating source, described methanol aqueous solution is made to become methanol steam, then it is transported to described methanol steam in combustion mechanism, make described methanol steam burn in described combustion mechanism.
In this method, described methanol steam generates carbon dioxide and water after burning in described combustion mechanism, owing to described methanol steam self has certain temperature, after described methanol steam is passed in described combustion mechanism, and can rapidly and sufficiently burn.And the described methanol steam of part can produce hydrogen during burning, the hydrogen being generated generates water with oxygen reaction (burning) immediately, makes described methanol steam discharge heat to greatest extent during burning.
In this method, in described evaporation device, described methanol aqueous solution contacts with the catalysis material containing copper, during the described methanol aqueous solution in described evaporation device is heated by described heating source, described catalysis material can make the described methanol aqueous solution of part generate hydrogen and carbon monoxide, that is described evaporation device does not contain only described methanol steam, possibly together with hydrogen and carbon monoxide.Described catalysis material is pure copper material or Cu alloy material, preferably select beryllium copper material, and during catalysis, the air pressure in described evaporation device is normal pressure, described catalysis material is arranged on temperature and arrives position between less than or equal to 300 degrees Celsius more than or equal to 200 degrees Celsius.
In this method, in beryllium copper material, according to percentage by weight, the weight percentage of beryllium is 5%-93%, and remaining is then copper；The weight percentage of beryllium is 8%-90%, and remaining is then copper；The weight percentage of beryllium is 10%-86%, and remaining is then copper；The weight percentage of beryllium is 15%-82%, and remaining is then copper；The weight percentage of beryllium is 19%-78%, and remaining is then copper；The weight percentage of beryllium is 24%-73%, and remaining is then copper；The weight percentage of beryllium is 29%-69%, and remaining is then copper；The weight percentage of beryllium is 33%-56%, and remaining is then copper；The weight percentage of beryllium is 41%-51%, and remaining is then copper；The weight percentage of beryllium is 45%-49%, and remaining is then copper.It is described methanol aqueous solution can be made when heating, can promptly produce the fuel gas such as substantial amounts of hydrogen and carbon monoxide that beryllium and copper select the benefit of above-mentioned weight percentage respectively.And the catalysis material that beryllium copper material contains copper with other is compared, described methanol aqueous solution is when heating, and the speed producing the imflammable gas such as hydrogen and carbon monoxide is fast, and the amount producing is many.
In this method, described evaporation device can use the material of cupric to make, then just not be used in described evaporation device and arranges described catalysis material, described evaporation device inherently described catalysis material.
In this method, described methanol aqueous solution in described evaporation device is directly or indirectly heated by described heating source, described methanol aqueous solution is directly heated by described heating source, refer to that described heating source directly heats described evaporation device, or described heating source directly heats described methanol aqueous solution, heating will be directly placed in described evaporation device by described heating source.Described methanol aqueous solution can also be heated by way of heat transfer by described heating source indirectly.
In this method, the heat of waste gas in the blast pipe of described combustion mechanism can also be utilized to heat described evaporation device, will described evaporation device be arranged on the position of described blast pipe；Or described evaporation device is arranged in described blast pipe, the heat in described blast pipe is allowed directly to heat described evaporation device, i.e. described evaporation device is arranged in the inner chamber of described blast pipe, or described blast pipe and described evaporation device are integrally formed i.e. formation evaporation exhaust gear, the inside of described evaporation exhaust gear is provided with evaporation cavity, and being provided with exhaust passage in the centre of described evaporation exhaust gear, described evaporation cavity is arranged on the surrounding of described exhaust passage.
In this method, in described methanol aqueous solution, first alcohol and water is mixed in the volume component ratio between 0.1:99.9-99.9:0.1, first alcohol and water is mixed in the volume component ratio between 10:90-90:10, first alcohol and water is mixed in the volume component ratio between 20:80-80:20, first alcohol and water is mixed in the volume component ratio between 30:70-70:30, and first alcohol and water is mixed in the volume component ratio between 40:60-60:40, and first alcohol and water is mixed in the volume component ratio of 1:1.First alcohol and water mixes according to above-mentioned volume component ratio, mixed described methanol aqueous solution can be made to produce substantial amounts of imflammable gas in described evaporation device, and discharge substantial amounts of heat when burning, moreover it is possible to save fuel.
In this method, the water in described methanol aqueous solution can use heavy water, and the benefit using heavy water is to produce substantial amounts of hydrogen during heating.Described combustion mechanism is boiler, internal combustion engine or gas-cooker.
Refer to Fig. 1, disclosed in described Fig. 1 is a kind of to utilize methanol aqueous solution as the burner of fuel, including evaporation device 2 and combustion mechanism 1, the venthole of described evaporation device 2 is connected with the fuel air pipe of described combustion mechanism 1 by air shooter 5, and described evaporation device 2 is arranged on the exhaust position of described combustion mechanism 1；When described combustion mechanism 1 works, the heat producing described exhaust position heats as heating source to the methanol aqueous solution in described evaporation device 2, making described methanol aqueous solution become methanol steam, described methanol steam is transported in described combustion mechanism 1 burning by described air shooter 5.
In the present embodiment, also including methyl alcohol water storage apparatus 3, described methyl alcohol water storage apparatus 3 is connected with the inlet opening of described evaporation device 2 by connecting tube 4, and described methyl alcohol water storage apparatus 3 is used for filling described methanol aqueous solution.
In the present embodiment, the blast pipe 11 of described combustion mechanism 1 is partially or completely surrounded by described evaporation device 2, and described evaporation device 2 and described blast pipe 11 are in laminating shape, and in order to absorb the heat lift temperature of waste gas, this is to heat by way of heat transfer.Described evaporation device 2 can be following structure: the first structure, is provided with groove (picture) on described evaporation device 2, and described blast pipe 11 is arranged in described groove；The second structure, described evaporation device 2 includes Part I (picture) and the Part II (picture) coordinating with described Part I, described Part I is provided with first and fixes groove (picture), fix at described Part II corresponding described first and be provided with second on the position of groove and fix groove (picture), when described blast pipe 11 is clamped by described Part I and described Part II, described blast pipe 11 is fixed on described first and fixes groove and described second and fix in groove；The third structure, described evaporation device 2 is evaporation tube, and the material containing copper that described evaporation tube uses is made, described evaporation tube is wrapped on the outer wall of described blast pipe 11 (shown in Figure 2), the liquid feeding end of described evaporation tube connects with described connecting tube 4, and the outlet side of described evaporation tube connects with described air shooter 5.
In the present embodiment, described evaporation device 2 can also be arranged in the blast pipe 11 of described combustion mechanism 1 (picture), in order to absorb the heat lift temperature of the waste gas in described blast pipe 11.Described evaporation device 2 is arranged in the blast pipe 11 of described combustion mechanism 1 two ways, and a kind of mode is that described evaporation device 2 is arranged in the inner chamber of described blast pipe 11, the inside of i.e. described blast pipe 11, and this is to heat by way of heat transfer；Another way is, described blast pipe 11 and described evaporation device 2 are integrally formed and i.e. form evaporation exhaust gear, the inside of described evaporation exhaust gear is provided with evaporation cavity, and it is provided with exhaust passage in the centre of described evaporation exhaust gear, described evaporation cavity is arranged on the surrounding of described exhaust passage, the inlet opening of described evaporation cavity connects with described connecting tube 4, and the venthole of described evaporation cavity connects with described air shooter 5.
In the present embodiment, described methyl alcohol water storage apparatus 3 can also be replaced by methyl alcohol bucket, water bucket and pump for forming predetermined liquids ratio, described methyl alcohol is installed in described methyl alcohol bucket, described water is installed in described water bucket, described pump for forming predetermined liquids ratio is in the described methyl alcohol in certain described methyl alcohol bucket of volume component ratio extraction and the described water in described water bucket, and described pump for forming predetermined liquids ratio is pumped into mixed described methanol aqueous solution in described evaporation device.
In the present embodiment, also including the catalysis material containing copper, described catalysis material is arranged in described evaporation device 2, and contacts with the described methanol aqueous solution in described evaporation device 2.Described catalysis material is pure copper material or Cu alloy material, preferably selects beryllium copper material.During the described methanol aqueous solution in described evaporation device 2 is heated by described heating source, described catalysis material can make the described methanol aqueous solution of part generate hydrogen and carbon monoxide, that is described evaporation device 2 does not contain only described methanol steam, possibly together with hydrogen and carbon monoxide.During catalysis, the air pressure in described evaporation device 2 is normal pressure, and described catalysis material is arranged on temperature and arrives position between less than or equal to 300 degrees Celsius more than or equal to 200 degrees Celsius.
In the present embodiment, in beryllium copper material, according to percentage by weight, the weight percentage of beryllium is 5%-93%, and remaining is then copper；The weight percentage of beryllium is 8%-90%, and remaining is then copper；The weight percentage of beryllium is 10%-86%, and remaining is then copper；The weight percentage of beryllium is 15%-82%, and remaining is then copper；The weight percentage of beryllium is 19%-78%, and remaining is then copper；The weight percentage of beryllium is 24%-73%, and remaining is then copper；The weight percentage of beryllium is 29%-69%, and remaining is then copper；The weight percentage of beryllium is 33%-56%, and remaining is then copper；The weight percentage of beryllium is 41%-51%, and remaining is then copper；The weight percentage of beryllium is 45%-49%, and remaining is then copper.It is described methanol aqueous solution can be made when heating, can promptly produce the fuel gas such as substantial amounts of hydrogen and carbon monoxide that beryllium and copper select the benefit of above-mentioned weight percentage respectively.And the catalysis material that beryllium copper material contains copper with other is compared, described methanol aqueous solution is when heating, and the speed producing the imflammable gas such as hydrogen and carbon monoxide is fast, and the amount producing is many.
In the present embodiment, described evaporation device 2 can use the material of cupric to make, then just not be used in described evaporation device 2 and arranges described catalysis material, described evaporation device 2 inherently described catalysis material.
In the present embodiment, described combustion mechanism 1 is boiler or internal combustion engine, and described fuel air pipe is inlet manifold.
In the present embodiment, in described methanol aqueous solution, first alcohol and water is mixed in the volume component ratio between 0.1:99.9-99.9:0.1, first alcohol and water is mixed in the volume component ratio between 10:90-90:10, first alcohol and water is mixed in the volume component ratio between 20:80-80:20, first alcohol and water is mixed in the volume component ratio between 30:70-70:30, and first alcohol and water is mixed in the volume component ratio between 40:60-60:40, and first alcohol and water is mixed in the volume component ratio of 1:1.First alcohol and water mixes according to above-mentioned volume component ratio, mixed described methanol aqueous solution can be made to produce substantial amounts of imflammable gas in described evaporation device, and discharge substantial amounts of heat when burning, moreover it is possible to save fuel.
In the present embodiment, the water in described methanol aqueous solution can use heavy water, and the benefit using heavy water is to produce substantial amounts of hydrogen during heating.
In the present embodiment, described methanol aqueous solution can produce methanol steam, hydrogen and carbon monoxide in described evaporation device 2, owing to these gases self have certain temperature, when these gases are transported in described combustion mechanism 1, the sufficiently burning that can arrive rapidly generates carbon dioxide and water, and the water producing after burning can be used to the cistern water supply of described combustion mechanism 1.During burning, the described methanol steam of part can produce hydrogen during burning, and the hydrogen being generated generates water with oxygen reaction (burning) immediately, makes described methanol steam discharge heat to greatest extent during burning.
The utility model is owing to have employed described evaporation device 2 and described combustion mechanism 1, described methanol aqueous solution in described evaporation device 2 is heated by described heating source, described methanol aqueous solution is made to become described methanol steam, then described methanol steam is transported in described combustion mechanism 1 burning, during burning, described methanol steam is as main fuel, and can generate carbon dioxide and water after combustion.Described heating source uses the heat of the described blast pipe 11 of in described combustion mechanism 1, so can reduce energy loss, maximally utilise the heat of waste gas in described blast pipe 11. described catalysis material can also be used in described evaporation device 2, described catalysis material is during heating, described methanol aqueous solution can be made to produce hydrogen and carbon monoxide, so advantageously in the burning completely of described methanol steam, release energy to greatest extent, there is simple in construction, pollution-free, zero-emission, burn completely, save the energy and reduce the advantages such as energy loss.
Claims (8)
1. one kind utilizes methanol aqueous solution as the burner of fuel, it is characterized in that: include evaporation device and combustion mechanism, the venthole of described evaporation device is connected with the fuel air pipe of described combustion mechanism by air shooter, and described evaporation device is arranged on the exhaust position of described combustion mechanism；During the work of described combustion mechanism, the heat producing described exhaust position heats as heating source to the methanol aqueous solution in described evaporation device, making described methanol aqueous solution become methanol steam, described methanol steam is transported in described combustion mechanism burning by described air shooter.
2. according to claim 1 utilize methanol aqueous solution as the burner of fuel, it is characterised in that: also including methyl alcohol water storage apparatus, described methyl alcohol water storage apparatus is connected with the inlet opening of described evaporation device by connecting tube.
3. according to claim 1 and 2 utilize methanol aqueous solution as the burner of fuel, it is characterized in that: the blast pipe of described combustion mechanism is partially or completely surrounded by described evaporation device, described evaporation device and described blast pipe are in laminating shape, in order to absorb the heat lift temperature of waste gas.
4. according to claim 1 and 2 utilize methanol aqueous solution as the burner of fuel, it is characterised in that: described evaporation device is arranged in the blast pipe of described combustion mechanism, in order to absorb the heat lift temperature of the waste gas in described blast pipe.
5. according to claim 1 and 2 utilize methanol aqueous solution as the burner of fuel, it is characterized in that: also include the catalysis material containing copper, described catalysis material is arranged in described evaporation device, and contacts with the described methanol aqueous solution in described evaporation device.
6. according to claim 5 utilize methanol aqueous solution as the burner of fuel, it is characterised in that: described catalysis material is pure copper material or Cu alloy material.
7. according to claim 6 utilize methanol aqueous solution as the burner of fuel, it is characterised in that: described Cu alloy material is beallon material.
8. according to claim 1 and 2 utilize methanol aqueous solution as the burner of fuel, it is characterised in that: described combustion mechanism is boiler or internal combustion engine.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620337815.3U CN205714420U (en) | 2016-04-21 | 2016-04-21 | Utilize methanol aqueous solution as the burner of fuel |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620337815.3U CN205714420U (en) | 2016-04-21 | 2016-04-21 | Utilize methanol aqueous solution as the burner of fuel |
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| CN205714420U true CN205714420U (en) | 2016-11-23 |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105736131A (en) * | 2016-04-21 | 2016-07-06 | 唐雨晨 | Combustion method and device adopting methanol aqueous solution as fuel |
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2016
- 2016-04-21 CN CN201620337815.3U patent/CN205714420U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105736131A (en) * | 2016-04-21 | 2016-07-06 | 唐雨晨 | Combustion method and device adopting methanol aqueous solution as fuel |
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