CN204006080U - Methanol gasifying machine - Google Patents
Methanol gasifying machine Download PDFInfo
- Publication number
- CN204006080U CN204006080U CN201420319047.XU CN201420319047U CN204006080U CN 204006080 U CN204006080 U CN 204006080U CN 201420319047 U CN201420319047 U CN 201420319047U CN 204006080 U CN204006080 U CN 204006080U
- Authority
- CN
- China
- Prior art keywords
- vaporizer
- heat conduction
- fountain
- fuel tank
- methyl alcohol
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 title claims abstract description 339
- 239000006200 vaporizer Substances 0.000 claims abstract description 64
- 238000002309 gasification Methods 0.000 claims abstract description 58
- 239000002828 fuel tank Substances 0.000 claims abstract description 49
- 239000007921 spray Substances 0.000 claims abstract description 11
- 239000007788 liquid Substances 0.000 claims description 30
- 238000000034 method Methods 0.000 abstract description 7
- 230000008569 process Effects 0.000 abstract description 3
- 239000007789 gas Substances 0.000 description 17
- 239000000446 fuel Substances 0.000 description 11
- 238000010438 heat treatment Methods 0.000 description 9
- 238000002347 injection Methods 0.000 description 8
- 239000007924 injection Substances 0.000 description 8
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 6
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 4
- 238000002485 combustion reaction Methods 0.000 description 4
- 239000003345 natural gas Substances 0.000 description 4
- 239000001301 oxygen Substances 0.000 description 4
- 229910052760 oxygen Inorganic materials 0.000 description 4
- 238000009835 boiling Methods 0.000 description 3
- 239000000945 filler Substances 0.000 description 3
- 239000012530 fluid Substances 0.000 description 3
- 230000008901 benefit Effects 0.000 description 2
- 239000003245 coal Substances 0.000 description 2
- 238000009841 combustion method Methods 0.000 description 2
- 239000002283 diesel fuel Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 230000008676 import Effects 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- 238000006424 Flood reaction Methods 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000002964 excitative effect Effects 0.000 description 1
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 238000003032 molecular docking Methods 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
- 238000009834 vaporization Methods 0.000 description 1
- 230000008016 vaporization Effects 0.000 description 1
Landscapes
- Spray-Type Burners (AREA)
Abstract
The utility model relates to equipment for gasification and gasification process.The sufficient methanol gasifying machine of a kind of methanol gasifying, comprise heat conduction fuel tank, gaseous methanol outlet and methyl alcohol front pump, in heat conduction fuel tank, be provided with heater, heat(ing) coil and several fountain vaporizers that are connected in series, one end of heat(ing) coil links together with methyl alcohol front pump, fountain vaporizer comprises that gasification chamber and one end are located in the shower in gasification chamber, the inner surface of gasification chamber forms gasification face, gasification chamber is provided with vaporizer outlet, one end that shower is positioned at outside gasification chamber is provided with vaporizer entrance, the part that is positioned at gasification chamber is provided with spray orifice, the vaporizer entrance of first fountain vaporizer in fountain vaporizer links together with the other end of heat(ing) coil, the vaporizer outlet of last fountain vaporizer links together with gaseous methanol outlet.The utility model has solved the problem that existing equipment for gasification can not make methyl alcohol fully gasify.
Description
Technical field
The utility model relates to equipment for gasification, relates in particular to a kind of methanol gasifying machine.
Background technology
The flame temperature of methyl alcohol reaches as high as 1100 DEG C of left and right, if flame temperature can reach 1200 DEG C of left and right under oxygen enrichment fully burns, and the temperature of flame core, internal flame and flame envelope increases successively, when flame envelope sufficient combustion, temperature is the highest, want to make that the combustion flame temperature of methyl alcohol is higher should shift to an earlier date preheating, after the adjusting methyl alcohol of science and the ratio of oxygen, burning will be very abundant in addition, and after the methyl alcohol under rich oxygen content fully burns, its fuel value and flame temperature can increase by 70% left and right.Tradition methyl alcohol burning is liquid burning, and burning very insufficient greatly reduces the performance of calorific value, and taste excitatory produces, and has both been unfavorable for environmental protection, is difficult to again make methyl alcohol to be used as the industrial combustion energy and popularizes.Gaseous methanol after vaporization both can burn separately and also can carry out blending with imflammable gas such as liquefied gas, natural gas or oxygen, further bring into play to greatest extent the burning benefit of methyl alcohol, its calorific value can compare favourably with natural gas completely, and its calorific value exceedes natural gas even to a certain extent.To be used for substituting optimal clean, the environmental protection new forms of energy of the industrial fuels such as liquefied gas, diesel oil, natural gas and coal 21 century, greatly reduce the production cost of enterprise, be using at present diesel oil, liquefied gas, coal, etc. as the save energy and reduce the cost first-selected energy-saving equipment of comprehensive transformation of the factory of main fuel and catering industry, can be the operating cost of enterprise's reduction by 35%-10% in various degree.After methanol gasifying, burn and need have gasifying machine to complete.The existing method that methyl alcohol is gasified is that the method that adopts heating to boil gasifies, and corresponding equipment for gasification is the structure of heating boiling type.As in China Patent No. being 032720823, Granted publication day be Augusts 25 in 2004 day, be called the equipment for gasification that discloses a kind of boiling type in the patent document of " a kind of light hydroxyl gasification installation ", this equipment for gasification heats, makes liquid to produce to the liquid that flows through coil pipe by conduction oil to gasify.This equipment for gasification has the following disadvantages while being used for gasification of methanol: gasification methyl alcohol can produce boiling phenomenon and cause in methanol gas containing methanol liquid, is also that methanol gasifying is not thorough; Conduction oil easily produces fuel injection event; Water in methanol gas can not be isolated.
Utility model content
The first object of the present utility model aims to provide the sufficient methanol gasifying machine of a kind of methanol gasifying, has solved the problem that existing equipment for gasification can not make methyl alcohol fully gasify.
The second object of the present utility model is intended to further improve on the basis of the first object and a kind ofly can prevents that conduction oil from producing the methanol gasifying machine of fuel injection event, has solved the existing gasification installation heating by conduction oil and can produce the problem of conduction oil fuel injection event.
The 3rd object of the present utility model be intended to further provide on the basis of the first object a kind of can be by isolated the liquid water in methanol gas methanol gasifying machine, can not be by isolated water problem while having solved existing equipment for gasification gasification of methanol.
Above technical problem solves by following technical proposal: a kind of methanol gasifying machine, comprise heat conduction fuel tank, be positioned at the gaseous methanol outlet of heat conduction fuel tank outside, be positioned at several fountain vaporizers that are connected in series of heat conduction fuel tank and the methyl alcohol front pump that outlet links together with heat(ing) coil one end, in described heat conduction fuel tank, be provided with heater and heat(ing) coil, described fountain vaporizer comprises that gasification chamber and one end are located in the shower in gasification chamber, the inner surface of described gasification chamber forms gasification face, described gasification chamber is provided with vaporizer outlet, one end that described shower is positioned at outside gasification chamber is provided with vaporizer entrance, the part that is positioned at gasification chamber is provided with spray orifice, the vaporizer entrance of first fountain vaporizer in described fountain vaporizer links together with the other end of described heat(ing) coil, the vaporizer outlet of last fountain vaporizer links together with described gaseous methanol outlet.When use, conduction oil is attached in heat conduction fuel tank, by heater, conduction oil is heated, liquid methanol enters heat(ing) coil and by heat-conducting oil heating under the effect of methyl alcohol front pump, then enter shower and spray on the inner surface (face gasifies) of gasification chamber through vaporizer import, gasification chamber is because the heating that is subject to conduction oil is in hot state, methyl alcohol on the gasification face that is sprayed onto is vaporized, in spray process, may cause methyl alcohol to have part not have vaporized phenomenon to produce owing to not encountering the factors such as heat that gasification face or gasification face provide is inadequate, now in the time entering next stage fountain vaporizer, methyl alcohol is further gasified and is improved temperature, finally making methanol gas enter combustion furnace with the condition of high temperature from gas methyl alcohol outlet outflow burns.Some fountain vaporizers of the application comprise the scheme of only having a vaporizer.Two or more fountain vaporizers are connected in parallel and are equal to a fountain vaporizer, and therefore several fountain vaporizers are adopted to series connection, mode series-parallel connection arranged side by side is also the application's the technical scheme being equal to together.
The utility model also comprises the heat conduction chamber that is positioned at heat conduction fuel tank top, described heat conduction chamber diapire inner surface is inclined, between described heat conduction chamber and heat conduction fuel tank, be communicated with by the first oil pipe and the second oil pipe, the upper port of described the first oil pipe is positioned at that heat conduction chamber diapire is high-end, lower port is positioned at heat conduction fuel tank roof, and the upper port of described the second oil pipe is positioned at heat conduction chamber diapire low side, lower port and is positioned at the below of the lower port of the first oil pipe.Can effectively prevent that conduction oil from producing fuel injection event.When conduction oil quality bad and produce when fuel injection event, oil enter through the first oil pipe heat conduction chamber by cooling go to boil, then dirty and in the second oil pipe is back to heat conduction fuel tank rapidly, thereby play the effect that prevents oil spout.
As preferably, described the first oil pipe is inclined.Can effectively prevent that conduction oil from producing false fuel injection event.
As preferably, the inclination angle of described the first oil pipe for degree be 45 °～60 °.Can either effectively prevent true and false fuel injection event.
As preferably, bottom, fountain vaporizer and the heat(ing) coil that described heater is positioned at heat conduction fuel tank is positioned at the top of heat conduction fuel tank, and the lower port of described the second oil pipe is positioned at the two below of fountain vaporizer and heat(ing) coil.Can fully heat the conduction oil that floods heat(ing) coil and fountain vaporizer, can prevent again conduction oil from can not add the bottom of heat conduction fuel tank to and cover heater and produce dry combustion method phenomenon (while oiling from top, due to the setting of coil pipe and fountain vaporizer, while being communicated with the spatial channel of heat conduction fuel tank top and the bottom compared with little, easily produce return-air and freely do not cause bottom to produce the phenomenon of dry combustion method without oil).
The utility model also comprises the heat conduction oil circulating pump that conduction oil is circulated between the lower space of heat conduction fuel tank and upper space.The existing customary means that fluid in same casing is heated is all consistent the temperature of container inner fluid various piece for the bottom that heater is placed on to container by the mode of fluid free convection, when the method is ceaselessly carried out heat loss (sponging when methanol gasifying) and has object to hinder mobile structure for top, the promptness of heat conduction can be poor.The technical program can overcome the problems referred to above, makes fountain vaporizer and heated coil in heat conduction fuel tank even, effectively stops conduction oil fuel injection event.
As preferably, described gaseous methanol exports being connected to the first gas-liquid separator.While avoiding device start, produce a small amount of liquid methanol because preheating is insufficient, what flow to burner uses fire end head.
As preferably, in the gasification chamber of last the fountain vaporizer in described fountain vaporizer, be provided with methyl alcohol and arrange residual outlet.Avoid methyl alcohol moisture, what flow to burner with methanol gas uses fire end head.Realize the 3rd utility model object.
As preferably, described methyl alcohol is arranged residual outlet to being connected to the second gas-liquid separator.
As preferably, described methyl alcohol front pump is governor impeller, and the port of export of described methyl alcohol front pump is provided with the first Pressure gauge.Can know in time methyl alcohol pressure and adjust to pressure to meet the requirements, while making liquid methanol access arrangement, steadily, flow speed stability, stops to occur methanol eddy phenomenon in gasification.
The utlity model has following advantage: can carry out fast gasification fully to methyl alcohol; Can make the methanol gas flowing out keep high temperature and few containing liquid methanol amount.
Brief description of the drawings
Fig. 1 is the structural representation of methanol gasifying machine.
Fig. 2 is the schematic diagram of fountain vaporizer.
In figure: heat conduction fuel tank 1, liquid level display 11, the first temperature indicator 12, heat conduction fuel tank roof 13, heater 2, heat(ing) coil 3, methyl alcohol front pump 4, the first pipeline 41, the first Pressure gauge 42, the first control valve 43, the second control valve 44, support 45, fountain vaporizer 5, vaporizer entrance 51, vaporizer outlet 52, methyl alcohol is arranged residual outlet 53, gasification chamber 54, the first pleated portions 541, conduction oil storage chamber 542, expand groove 543, shower 55, the second pleated portions 551, methyl alcohol storage chamber 552, shower connects the position 553 of adjacent the second pleated portions, spray orifice 56, shower is towards one end 57 of vaporizer outlet, gaseous methanol outlet 6, second pipe 61, the 3rd control valve 62, the 7th control valve 63, the first gas-liquid separator 64, heat conduction oil circulating pump 7, the 3rd pipeline 71, the 4th pipeline 72, the 5th control valve 73, heat conduction chamber 8, heat conduction chamber diapire 81, the second oil pipe 82, oil filler 83, the 6th control valve 84, Safety relief valve 85, the 3rd Pressure gauge 86, the first oil pipe 87, the second gas-liquid separator 9, the 4th control valve 91, the second Pressure gauge 92, the 8th control valve 93.
Detailed description of the invention
Below in conjunction with accompanying drawing and embodiment, the utility model is further described.
Referring to Fig. 1, a kind of methanol gasifying machine, comprises heat conduction fuel tank 1, heater 2, heat(ing) coil 3, methyl alcohol front pump 4, fountain vaporizer 5, gaseous methanol outlet 6, heat conduction oil circulating pump 7 and heat conduction chamber 8.
Heat conduction fuel tank 1 is provided with liquid level display 11 and the first temperature indicator 12.
Heater 2 is positioned at the lower end of heat conduction fuel tank 1 inside.
Heat(ing) coil 3 is positioned at the upper end of heat conduction fuel tank 1 inside.The entrance point of heat(ing) coil 3 is docking together with the port of export of methyl alcohol front pump 4 with crossing the first pipeline 41.The first pipeline 41 is provided with the first Pressure gauge 42 and the first control valve 43.The first control valve 43 is ball valve.
Methyl alcohol front pump 4 is positioned at the outside of heat conduction fuel tank 1.Methyl alcohol front pump 4 is governor impeller.It is more specifically manual governing pump.The entrance point of methyl alcohol front pump 4 is provided with the second control valve 44.The second control valve 44 is ball valve.Methyl alcohol front pump 4 is arranged on support 45.
Fountain vaporizer 5 is positioned at the inner upper end of heat conduction fuel tank 1.Fountain vaporizer 5 has 5.Fountain vaporizer 5 is provided with vaporizer entrance 51 and vaporizer outlet 52.5 fountain vaporizers 5 are connected in series.The vaporizer entrance of first fountain vaporizer in 5 fountain vaporizers 5 (in figure low order end that) links together with the port of export of heat(ing) coil 3.The vaporizer outlet of last the fountain vaporizer in 5 fountain vaporizers 5 links together with gaseous methanol outlet 6 by second pipe 61.Second pipe 61 is provided with the first gas-liquid separator 64 and the 3rd control valve 62.The gas vent of the first gas-liquid separator 64 forms gaseous methanol outlet 6.The liquid outlet of the first gas-liquid separator 64 is provided with the 7th control valve 63.The 3rd control valve 62 is flanged ball valve.Gaseous methanol outlet 6, the first gas-liquid separator 64 and the 3rd control valve 62 are all positioned at the outside of heat conduction fuel tank 1.
Last fountain vaporizer in 5 fountain vaporizers 5 is provided with methyl alcohol and arranges residual outlet 53.Methyl alcohol is arranged residual outlet 53 and is linked together with the second gas-liquid separator 9.Methyl alcohol is arranged and between residual outlet 53 and the second gas-liquid separator 9, is provided with the 4th control valve 91 and the second Pressure gauge 92.The 4th control valve 91 is ball valve.The liquid outlet of the second gas-liquid separator 9 is provided with the 8th control valve 93.
Heat conduction oil circulating pump 7 is positioned at the outside of heat conduction fuel tank 1.The entrance point of heat conduction oil circulating pump 7 is communicated with the lower space (being the position at heater place) of heat conduction fuel tank 1 by the 3rd pipeline 71.The port of export of heat conduction oil circulating pump 7 is communicated with the upper space (being the position at fountain heating clamber place) of heat conduction fuel tank 1 by the 4th pipeline 72.The 3rd pipeline 71 is provided with the 5th control valve 73.The 5th control valve 73 is ball valve.
Heat conduction chamber 8 is positioned at the outside top of heat conduction fuel tank 1.Heat conduction chamber diapire 81 inner surfaces are inclined.Between heat conduction chamber 8 and heat conduction fuel tank 1, be communicated with by the first oil pipe 87 and the second oil pipe 82.It is high-end that the upper port of the first oil pipe 87 is positioned at heat conduction chamber diapire 81.The lower port of the first oil pipe 81 is positioned at heat conduction fuel tank roof 13.The first oil pipe 87 is inclined.The angle of inclination of the first oil pipe 87 is 45 °～60 °.The upper port of the second oil pipe 82 is positioned at heat conduction chamber diapire 81 low sides.The lower port of the second oil pipe 82 is positioned at the position below heat conduction fuel tank 1 middle part, is in the present embodiment between heater 2 and fountain vaporizer 5.Heat conduction chamber 8 is provided with oil filler 83, the 6th control valve 84, Safety relief valve 85 and the 3rd Pressure gauge 86.Safety relief valve 85 can avoid the interior conduction oil circulation time of heat conduction fuel tank 1, produce that gas cannot discharge and the security incident that causes.
Referring to Fig. 2, fountain vaporizer 5 comprises gasification chamber 54 and shower 55.The inner surface of gasification chamber 54 forms gasification face.Vaporizer outlet 52 is arranged at gasification chamber 54.In the time being provided with the remaining outlet of methyl alcohol, the remaining outlet of methyl alcohol is arranged at gasification chamber 54.Shower 55 one end are located in gasification chamber 54.Vaporizer import 51 is arranged in the part that shower 55 is positioned at gasification chamber 54 outsides.The part that shower 55 is positioned at gasification chamber is provided with some spray orifices 56.Shower does not arrange spray orifice towards one end 57 of vaporizer outlet for enclosed construction, can preferably avoid like this liquid methanol not to be vaporized and flows out gasification chamber.
Spray orifice 56 for diameter be the hole of 1～1.5 millimeter.The space distance of spray orifice 56 is 18～22mm.This physical dimension relation can improve the gasification result of methyl alcohol.
The method that methyl alcohol is gasified is:
Referring to Fig. 1, the first step, through oil filler 83 filling heat-conductive oil, conduction oil flows in heat conduction fuel tank 1 through Heat Room 8, the first oil pipe 87 and the second oil pipe 82.The temperature of conduction oil is 320～350 DEG C.The addition of conduction oil is can flood fountain vaporizer 5 and heat exchange coil 3 and above heat conduction fuel tank 1, leave space and not exclusively fill heat conduction fuel tank.
Second step, by heater 2 by heat-conducting oil heating to 200～220 DEG C in heat conduction fuel tank 1.Whether observe temperature by temperature indicator 12 reaches.In the process of heating, open the 5th control valve 73 and by heat conduction oil circulating pump 7, the conduction oil in heat conduction fuel tank 1 circulated.
The 3rd step: first open the first control valve 43, the second control valve 44, the 4th control valve 92 and methyl alcohol front pump 4, then open the 3rd control valve 62.Methyl alcohol is input to heat(ing) coil 3 by methyl alcohol front pump 4, when methyl alcohol flows through heat(ing) coil 3 by heat-conducting oil heating.
Referring to Fig. 2, the inner surface that the methyl alcohol of heat is ejected into gasification chamber 54 through spray orifice 56 from vaporizer entrance 51 enters shower 55 is on gasification face and be vaporized.Gas methyl alcohol and the methyl alcohol fully not gasified flow out through vaporizer outlet 52.
Referring to Fig. 1, then flow to next fountain vaporizer 5, the like, last gas (if contain water in methyl alcohol, gas is methanol gas and water vapour) flows out to burner from gaseous methanol outlet 6 after the first gas-liquid separator 64 separates.Containedly in methyl alcohol do not arranged after residual outlet 53 is discharged in the second gas-liquid separator 9 by gas-liquid separation and discharge through methyl alcohol by residues such as the water of gas.
Claims (10)
1. a methanol gasifying machine, comprise heat conduction fuel tank and the gaseous methanol outlet that is positioned at heat conduction fuel tank outside, in described heat conduction fuel tank, be provided with heater and heat(ing) coil, it is characterized in that, also comprise and be positioned at several fountain vaporizers that are connected in series of heat conduction fuel tank and the methyl alcohol front pump that outlet links together with heat(ing) coil one end, described fountain vaporizer comprises that gasification chamber and one end are located in the shower in gasification chamber, the inner surface of described gasification chamber forms gasification face, described gasification chamber is provided with vaporizer outlet, one end that described shower is positioned at outside gasification chamber is provided with vaporizer entrance, the part that is positioned at gasification chamber is provided with spray orifice, the vaporizer entrance of first fountain vaporizer in described fountain vaporizer links together with the other end of described heat(ing) coil, the vaporizer outlet of last fountain vaporizer links together with described gaseous methanol outlet.
2. methanol gasifying machine according to claim 1, it is characterized in that, also comprise the heat conduction chamber that is positioned at heat conduction fuel tank top, described heat conduction chamber diapire inner surface is inclined, between described heat conduction chamber and heat conduction fuel tank, be communicated with by the first oil pipe and the second oil pipe, the upper port of described the first oil pipe is positioned at that heat conduction chamber diapire is high-end, lower port is positioned at heat conduction fuel tank roof, and the upper port of described the second oil pipe is positioned at heat conduction chamber diapire low side, lower port and is positioned at the below of the lower port of the first oil pipe.
3. methanol gasifying machine according to claim 2, is characterized in that, described the first oil pipe is inclined.
4. methanol gasifying machine according to claim 3, is characterized in that, the inclination angle of described the first oil pipe is 45 °～60 ° for spending.
5. according to the methanol gasifying machine described in claim 2 or 3 or 4, it is characterized in that, bottom, fountain vaporizer and the heat(ing) coil that described heater is positioned at heat conduction fuel tank is positioned at the top of heat conduction fuel tank, and the lower port of described the second oil pipe is positioned at the two below of fountain vaporizer and heat(ing) coil.
6. methanol gasifying machine according to claim 5, is characterized in that, also comprises the heat conduction oil circulating pump that conduction oil is circulated between the lower space of heat conduction fuel tank and upper space.
7. according to the methanol gasifying machine described in claim 1 or 2 or 3 or 4, it is characterized in that, described gaseous methanol exports being connected to the first gas-liquid separator.
8. according to the methanol gasifying machine described in claim 1 or 2 or 3 or 4, it is characterized in that, in the gasification chamber of last the fountain vaporizer in described fountain vaporizer, be provided with methyl alcohol and arrange residual outlet.
9. methanol gasifying machine according to claim 8, is characterized in that, described methyl alcohol is arranged residual outlet to being connected to the second gas-liquid separator.
10. according to the methanol gasifying machine described in claim 1 or 2 or 3 or 4, it is characterized in that, described methyl alcohol front pump is governor impeller, and the port of export of described methyl alcohol front pump is provided with the first Pressure gauge.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420319047.XU CN204006080U (en) | 2014-06-16 | 2014-06-16 | Methanol gasifying machine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420319047.XU CN204006080U (en) | 2014-06-16 | 2014-06-16 | Methanol gasifying machine |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204006080U true CN204006080U (en) | 2014-12-10 |
Family
ID=52046077
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420319047.XU Expired - Lifetime CN204006080U (en) | 2014-06-16 | 2014-06-16 | Methanol gasifying machine |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204006080U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104214791A (en) * | 2014-06-16 | 2014-12-17 | 汤伟荣 | Methanol gasifying machine and methanol gasifying method |
-
2014
- 2014-06-16 CN CN201420319047.XU patent/CN204006080U/en not_active Expired - Lifetime
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104214791A (en) * | 2014-06-16 | 2014-12-17 | 汤伟荣 | Methanol gasifying machine and methanol gasifying method |
| CN104214791B (en) * | 2014-06-16 | 2016-07-20 | 汤伟荣 | Methanol gasifying machine and methanol gasifying method |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN104456605B (en) | Gasification device for ordinary-pressure liquid light hydrocarbons | |
| CN203240576U (en) | Alcohol-based fuel burner | |
| CN104214791B (en) | Methanol gasifying machine and methanol gasifying method | |
| CN204006080U (en) | Methanol gasifying machine | |
| CN201803385U (en) | Quick ignition gasification furnace adopting alcoholic groups as liquid fuels | |
| CN202598619U (en) | Kitchen range using alcohol-group fuel | |
| CN205825017U (en) | A kind of methanol kitchen range and methanol cooking stove thereof | |
| CN204006079U (en) | Jet proof type conduction oil box structure | |
| CN104696982A (en) | Coal-fired stove with vapor supported combustion function | |
| CN204006081U (en) | Methanol gasifying structure | |
| CN205351308U (en) | Vertical methanol combustion device | |
| CN205351309U (en) | Horizontal methanol combustion device | |
| CN103196138A (en) | Alcohol group fuel burner | |
| CN204313272U (en) | The alcohol radical combusting vaporization formula stove core improved | |
| CN207122897U (en) | The combustion furnace of high-efficiency environment friendly | |
| CN203478184U (en) | Biomass vapor generator | |
| CN203349267U (en) | Novel double-high burner | |
| CN206145732U (en) | Automatic inhale mellow wine gasification kitchen | |
| CN201903086U (en) | Liquid fuel combustion device | |
| CN201944900U (en) | Liquid fuel gasification device | |
| CN201672574U (en) | Alcohol base liquid fuel gasifying device | |
| CN205979897U (en) | From vaporization alcohol group fuel -fired furnace | |
| CN203893175U (en) | Alcohol-based fuel stove core and energy-efficient gasification stove comprising same | |
| CN103307597A (en) | Gasification-type oven core adopting alcohol-based fuel | |
| CN105135429B (en) | A kind of burner and its combustion method for cracking gasification |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CX01 | Expiry of patent term | ||
| CX01 | Expiry of patent term |
Granted publication date: 20141210 |