CN201695003U - Biomass fixed-bed gasification furnace - Google Patents
Biomass fixed-bed gasification furnace Download PDFInfo
- Publication number
- CN201695003U CN201695003U CN 201020150512 CN201020150512U CN201695003U CN 201695003 U CN201695003 U CN 201695003U CN 201020150512 CN201020150512 CN 201020150512 CN 201020150512 U CN201020150512 U CN 201020150512U CN 201695003 U CN201695003 U CN 201695003U
- Authority
- CN
- China
- Prior art keywords
- heater
- agent inlet
- inlet
- gasification agent
- pyrolysis tube
- 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
Images
Landscapes
- Processing Of Solid Wastes (AREA)
Abstract
The utility model provides the technical scheme of a biomass fixed-bed gasification furnace, which is characterized in that at least one pyrolyzing barrel made of a high-temperature resistant material is arranged on a furnace body, the axial line of each pyrolyzing barrel is vertical to the cross section of the furnace body, a raw material inlet is arranged at the upper open end of each pyrolyzing barrel and is higher than the upper top end of the furnace body, and the lower open end of each pyrolyzing barrel is positioned at the middle part in the furnace body; a gas reformer is arranged between the circumference of each pyrolyzing barrel and the inner wall of the furnace body, the inner cavity of the furnace body is divided into an upper part and a lower part through the gas reformer, and a combustion gas cavity is arranged at the upper part, and a combustion cavity is arranged at the lower part; a product gas outlet is communicated with the combustion gas cavity; a gasifying agent inlet is provided with a primary gasifying agent inlet, a secondary gasifying agent inlet and a tertiary gasifying agent inlet, wherein the primary gasifying agent inlet and the raw material inlet are the same inlet, the secondary gasifying agent inlet is positioned at the bottom of the furnace body and communicated with the hollow cavity at the lower part of a grate, and the tertiary gasifying agent inlet is connected with a gas-distributing ring with a nozzle in the combustion cavity; and a plurality of reforming passages for connecting the combustion gas cavity and the combustion cavity are arranged in the gas reformer.
Description
Technical field:
The utility model relates to a kind of equipment that utilizes carbonaceous material production combustion gas, especially a kind of biomass fixed-bed gasification furnace.
Background technology:
In the prior art, technique known is that our unit is in application of Patent Office of State Intellectual Property Office and disclosed No. 200710113113.2 patent applications, this patent application discloses a kind of technical scheme of method and apparatus of preparing synthesized gas by biomass step-wise rich oxygen gasification, vapourizing furnace in the technical scheme is to adopt the downdraft fixed-bed structure, whole device can produce the synthetic gas of high quality as synthol effectively, but, this device is the system and device that is combined into by a plurality of equipment, so its complex structure, and pyrolysis also needs external heat source, and this is the existing in prior technology weak point.
Summary of the invention:
The purpose of this utility model is exactly at the existing in prior technology deficiency, and provide a kind of technical scheme of biomass fixed-bed gasification furnace, this scheme adopts the fixed-bed type structure, dry thermal cracking, burning reduction and gas reforming several steps that gasifying biomass is experienced are all finished in a body of heater, make the structure of aerogenesis become succinct, simple in equipment need not external heat source, and can obtain to contain hardly the high-quality product gas of tar.
This programme is realized by following technical measures: the body of heater that includes the band thermal insulation layer, material inlet, product gas outlet and gasification agent inlet are arranged on body of heater, in the bottom of body of heater fire grate and ash output hole are arranged, the characteristics of this programme are to have a pyrolysis tube of being made by high temperature material on described body of heater at least, the cross section of the axis normal body of heater of each pyrolysis tube, the upper open end of each pyrolysis tube is a material inlet, and exceeding the last top of body of heater, the lower open end of described each pyrolysis tube is positioned at the intravital middle part of stove; Around described each pyrolysis tube and between the inboard wall of furnace body gas reforming device is arranged, this gas reforming device is separated into two portions up and down with the body of heater inner chamber, and top is the combustion gas chamber, and the bottom is a burning chamber; Described product gas outlet communicates with the combustion gas chamber; Described gasification agent inlet is gasification agent inlet, second gasification agent inlet and three gasification agent inlets once, gasification agent inlet and material inlet are same inlet, second gasification agent inlet is positioned at bottom of furnace body and communicates with the cavity of fire grate bottom, and three times gasification agent inlet is connected with the branch compression ring of band nozzle in the burning chamber; Many the reformation passages that connect combustion gas chamber and burning chamber are arranged in described gas reforming device.The concrete characteristics of this programme also have, and the position of described minute compression ring is on the top of burning chamber, below each pyrolysis tube lower open end.The plane of a loop of described minute compression ring and the transverse cross-section parallel of body of heater.Described reformation passage is vertical passage, or the passage that tilts, or crooked passage.Described gas reforming device is to make with high temperature material.The position of described gas reforming device is the middle and lower part at the pyrolysis tube.Nozzle on described minute compression ring has two at least, and the injection direction of each nozzle all is to be tilted to injection.
The beneficial effect of this programme can be learnt according to the narration to such scheme, owing to have a pyrolysis tube of making by high temperature material at least on the body of heater in this scheme, the cross section of the axis normal body of heater of each pyrolysis tube, the upper open end of each pyrolysis tube is a material inlet, and exceeding the last top of body of heater, the lower open end of described each pyrolysis tube is positioned at the intravital middle part of stove; Around described each pyrolysis tube and between the inboard wall of furnace body ring-type gas reforming device is arranged, this gas reforming device is separated into two portions up and down with the body of heater inner chamber, and top is the combustion gas chamber, and the bottom is a burning chamber; Described product gas outlet communicates with the combustion gas chamber; Described gasification agent inlet is gasification agent inlet, second gasification agent inlet and three gasification agent inlets once, gasification agent inlet and material inlet are same inlet, second gasification agent inlet is positioned at bottom of furnace body and communicates with the cavity of fire grate bottom, and three times gasification agent inlet is connected with the branch compression ring of band nozzle in the burning chamber; Many the reformation passages that connect combustion gas chamber and burning chamber are arranged in described gas reforming device.This structure is when operation, biomass material is added by material inlet, in the pyrolysis tube falls into burning chamber and pyrolysis tube on the fire grate, raw material in the pyrolysis tube is by the heating of the high-temperature fuel gas more than 1000 ℃ in the gas reforming device, dry thermal cracking takes place and also be that the vaporized chemical that gasification agent inlet enters carries out the partial gasification reaction by material inlet, raw material behind pyrolysis and partial gasification enters burning chamber, with the vaporized chemical that is entered by second gasification agent inlet the burning reduction reaction takes place, the raw material that has reacted becomes ash and is discharged outside the body of heater by ash output hole.By the gaseous state thing that produces through pyrolysis and partial gasification in the pyrolysis tube, with the gaseous state thing that produces through the burning reduction in the burning chamber, mix the combustion reactions of generation incomplete oxidation with three gasification agent inlets through minute vaporized chemical of compression ring upper spray nozzle ejection and generate combustion gas, the reformation passage of while in the gas reforming device, tar in the combustion gas is carried out the High-Temperature Strengthening cracking, eliminate the tar in the combustion gas, and gaseous constituent reformed, when combustion gas entered the combustion gas chamber, the high-quality product gas that has just become to contain hardly tar was discharged by product gas outlet.By above-mentioned operational process as can be known, as long as control the quantity of input biomass material and the ratio of each gasification agent inlet input vaporized chemical well,, thereby also just can control product makings amount and the composition of being produced with regard to the temperature and the reaction depth of each one in the may command body of heater.This programme is the advantage separately that has absorbed downdraft fixed-bed gasification furnace and updraft type fixed-bed gasification furnace, by dry thermal cracking, burning reduction and gas reforming several steps a body of heater in the proceed step by step of subregion with raw material, make the structure of aerogenesis become succinct, the equipment structure is compact simple, and do not need external heat source, adaptable raw material range is wide, the transformation efficiency height of carbon, can obtain to contain hardly the high-quality product gas of tar, can regulate the ratio of various active principles in the product gas as required, prevent to produce the secondary pollution of tar liquid.This shows that the utility model compared with prior art has substantive distinguishing features and progress, the beneficial effect of its enforcement also is conspicuous.
Description of drawings:
Fig. 1 is the part sectional structure synoptic diagram of first embodiment of the utility model.
Fig. 2 is the A-A sectional structure synoptic diagram of Fig. 1.
Fig. 3 is the part sectional structure synoptic diagram of second embodiment of the utility model.
Fig. 4 is the B-B sectional structure synoptic diagram of Fig. 2.
Among the figure, 1 is second gasification agent inlet, and 2 is fire grate, 3 is body of heater, and 4 is the gas reforming device, and 5 are the pyrolysis tube, 6 is material inlet, and 7 is thermal insulation layer, and 8 is product gas outlet, 9 are the combustion gas chamber, and 10 are the reformation passage, and 11 is three gasification agent inlets, 12 for dividing compression ring, 13 is burning chamber, and 14 is ash output hole, and 15 is nozzle.
Embodiment:
For clearly demonstrating the technical characterstic of this programme,, and, this programme is set forth in conjunction with its accompanying drawing below by two embodiments.
First embodiment can be found out by attached Fig. 1 and 2, the biomass fixed-bed gasification furnace of this programme has the body of heater 3 of band thermal insulation layer 7, material inlet 6, product gas outlet 8 and gasification agent inlet are arranged on body of heater 3, fire grate 2 and ash output hole 14 are arranged in the bottom of body of heater 3, this programme be on described body of heater 3 with the body of heater 3 coaxial pyrolysis tubes 5 that a steel cylindrical drum is arranged, the upper open end of this pyrolysis tube 5 is a material inlet 6, and exceeding the last top of body of heater 3, the lower open end of described pyrolysis tube 5 is positioned at the middle part of body of heater 3.Described pyrolysis tube 5 has a ring-type gas reforming device 4 on every side and between body of heater 3 inwalls, the position of this gas reforming device 4 is the middle and lower parts at pyrolysis tube 5, described gas reforming device 4 is to make with high temperature material, and what this embodiment adopted is to be built into refractory brick.Many the reformation path 10s that connect combustion gas chamber 9 and burning chamber 13 are arranged in described gas reforming device 4, and described reformation path 10 can adopt vertical passage, or the passage that tilts, or crooked passage, and what this embodiment adopted is vertical channel.Described gas reforming device 4 is divided into two portions up and down with body of heater 3 inner chamber fire grates 2 tops, and top is combustion gas chamber 9, and the bottom is a burning chamber 13.Described product gas outlet 8 communicates with combustion gas chamber 9.Described gasification agent inlet is gasification agent inlet once, 1 and three gasification agent inlet 11 of second gasification agent inlet, gasification agent inlet and material inlet 6 are same inlet, second gasification agent inlet 1 is positioned at body of heater 3 bottoms and communicates with the cavity of fire grate 2 bottoms, three times gasification agent inlet 11 is connected with the branch compression ring 12 of band nozzle 15 in the burning chamber 13, the position of described minute compression ring 12 is on the top of burning chamber 13, below pyrolysis tube 5 lower open ends, the transverse cross-section parallel of the plane of a loop of described minute compression ring 12 and body of heater 3, nozzle 5 on described minute compression ring 12 has two at least, the injection direction of each nozzle 15 all is to be tilted to injection, and the nozzle 15 that this embodiment adopts is four.
Thermal insulation layer described in this programme on the body of heater also can adopt the thermal insulation layer that has water jacket, and more having increased vapourizing furnace can also provide steam and hot water in aerogenesis, enlarged its function.
Second embodiment can be found out by accompanying drawing 3 and 4, the biomass fixed-bed gasification furnace of this programme has the body of heater 3 of band thermal insulation layer 7, material inlet 6 is arranged on body of heater 3, product gas outlet 8 and gasification agent inlet, fire grate 2 and ash output hole 14 are arranged in the bottom of body of heater 3, this programme is for adapting to the vapourizing furnace of large-scale gas equipment, so three pyrolysis tubes of being made by high temperature material potter's clay 5 are arranged on described body of heater 3, the cross section of the axis normal body of heater 3 of three pyrolysis tubes 5, the upper open end of three pyrolysis tubes 5 is three material inlets 6, and exceeding the last top of body of heater 3, the lower open end of described three pyrolysis tubes 5 is positioned at the middle part of body of heater 3.Described three pyrolysis tubes 5 have a gas reforming device 4 on every side and between body of heater 3 inwalls, the position of this gas reforming device 4 is the middle and lower parts at each pyrolysis tube 5, described gas reforming device 4 is to make with high temperature material, and what this embodiment adopted is to make with refractory mortar.Many the reformation path 10s that connect combustion gas chamber 9 and burning chamber 13 are arranged in described gas reforming device 4, and described reformation path 10 can adopt vertical passage, or the passage that tilts, or crooked passage, and what this embodiment adopted is ramp way.Described gas reforming device 4 is divided into two portions up and down with body of heater 3 inner chamber fire grates 2 tops, and top is combustion gas chamber 9, and the bottom is a burning chamber 13.Described product gas outlet 8 communicates with combustion gas chamber 9.Described gasification agent inlet is gasification agent inlet once, 1 and three gasification agent inlet 11 of second gasification agent inlet, gasification agent inlet is three material inlets 6 just, second gasification agent inlet 1 is positioned at body of heater 3 bottoms and communicates with the cavity of fire grate 2 bottoms, three times gasification agent inlet 11 is connected with the branch compression ring 12 of band nozzle 15 in the burning chamber 13, the position of described minute compression ring 12 is on the top of burning chamber 13, below each pyrolysis tube 5 lower open end, the transverse cross-section parallel of the plane of a loop of described minute compression ring 12 and body of heater 3, nozzle 5 on described minute compression ring 12 has two at least, the injection direction of each nozzle 15 all is to be tilted to injection, and the nozzle 15 that this embodiment adopts is nine.
Claims (9)
1. biomass fixed-bed gasification furnace, include the body of heater of band thermal insulation layer, material inlet, product gas outlet and gasification agent inlet are arranged on body of heater, in the bottom of body of heater fire grate and ash output hole are arranged, it is characterized in that: have a pyrolysis tube of being made by high temperature material on described body of heater at least, the cross section of the axis normal body of heater of each pyrolysis tube, the upper open end of each pyrolysis tube are material inlet, and exceeding the last top of body of heater, the lower open end of described each pyrolysis tube is positioned at the intravital middle part of stove; Around described each pyrolysis tube and between the inboard wall of furnace body gas reforming device is arranged, this gas reforming device is separated into two portions up and down with the body of heater inner chamber, and top is the combustion gas chamber, and the bottom is a burning chamber; Described product gas outlet communicates with the combustion gas chamber; Described gasification agent inlet is gasification agent inlet, second gasification agent inlet and three gasification agent inlets once, gasification agent inlet and material inlet are same inlet, second gasification agent inlet is positioned at bottom of furnace body and communicates with the cavity of fire grate bottom, and three times gasification agent inlet is connected with the branch compression ring of band nozzle in the burning chamber; Many the reformation passages that connect combustion gas chamber and burning chamber are arranged in described gas reforming device.
2. vapourizing furnace according to claim 1 is characterized in that: the position of described minute compression ring is on the top of burning chamber, below each pyrolysis tube lower open end.
3. vapourizing furnace according to claim 1 and 2 is characterized in that: the plane of a loop of described minute compression ring and the transverse cross-section parallel of body of heater.
4. vapourizing furnace according to claim 1 is characterized in that: described reformation passage is vertical passage.
5. vapourizing furnace according to claim 1 is characterized in that: described reformation passage is the passage that tilts.
6. vapourizing furnace according to claim 1 is characterized in that: described reformation passage is crooked passage.
7. vapourizing furnace according to claim 1 is characterized in that: described gas reforming device is to make with high temperature material.
8. according to claim 1 or 7 described vapourizing furnaces, it is characterized in that: the position of described gas reforming device is the middle and lower part at each pyrolysis tube.
9. vapourizing furnace according to claim 3 is characterized in that: the nozzle on described minute compression ring has two at least, and the injection direction of each nozzle all is to be tilted to injection.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201020150512 CN201695003U (en) | 2010-04-06 | 2010-04-06 | Biomass fixed-bed gasification furnace |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201020150512 CN201695003U (en) | 2010-04-06 | 2010-04-06 | Biomass fixed-bed gasification furnace |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201695003U true CN201695003U (en) | 2011-01-05 |
Family
ID=43396244
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201020150512 Expired - Lifetime CN201695003U (en) | 2010-04-06 | 2010-04-06 | Biomass fixed-bed gasification furnace |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201695003U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101805635A (en) * | 2010-04-06 | 2010-08-18 | 山东省科学院能源研究所 | Biomass fixed bed gasification furnace |
| CN102134071A (en) * | 2011-04-01 | 2011-07-27 | 大连理工大学 | Method for preparing activated carbon by pyrolysis of organic matters |
-
2010
- 2010-04-06 CN CN 201020150512 patent/CN201695003U/en not_active Expired - Lifetime
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101805635A (en) * | 2010-04-06 | 2010-08-18 | 山东省科学院能源研究所 | Biomass fixed bed gasification furnace |
| CN101805635B (en) * | 2010-04-06 | 2012-10-03 | 山东省科学院能源研究所 | Biomass fixed bed gasification furnace |
| CN102134071A (en) * | 2011-04-01 | 2011-07-27 | 大连理工大学 | Method for preparing activated carbon by pyrolysis of organic matters |
| CN102134071B (en) * | 2011-04-01 | 2012-08-22 | 大连理工大学 | Method for preparing activated carbon by pyrolysis of organic matters |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN101805638B (en) | Biomass gasification method | |
| CN101144022B (en) | Three-section type biomass gasifying furnace | |
| CN102329656B (en) | Downdraft biomass gasification reaction chamber and gasification process thereof | |
| CN101693848A (en) | Process for internally heated continuous preparing biomass pyrolysis gasification gas and rotary furnace utilized by same | |
| CN201530810U (en) | Rotary furnace used in method for continuously preparing biomass pyrolysis gasification gas in internal heat mode | |
| CN204237743U (en) | A kind of New type coal gas retort | |
| CN101230281A (en) | Solid biomass semi-water coal-gas producer | |
| CN102796568B (en) | Device and technology for producing blau-gas and carbon monoxide | |
| CN101805635B (en) | Biomass fixed bed gasification furnace | |
| CN107083249A (en) | A kind of fine coal prepares air flow bed pyrolysis oven, the system and method vented one's spleen rich in methane thermal | |
| CN201695003U (en) | Biomass fixed-bed gasification furnace | |
| CN105861055B (en) | The reaction unit of synthesis gas is prepared for methane and carbon dioxide catalytic reforming | |
| CN113652508A (en) | Electromagnetic induction heating reforming furnace and using method thereof | |
| CN102443445B (en) | Process and device for continuously gasifying biomass and simultaneously removing tar in moving bed | |
| CN102226106A (en) | Biomass vapourizing furnace | |
| CN202754974U (en) | Internal heat exchange type hydrogenation gasification furnace | |
| CN206736188U (en) | A kind of three-stage gasification furnace | |
| CN100503437C (en) | Reaction furnace for manufacturing carbon disulfide using high pressure non catalytic natural gas method | |
| CN206902071U (en) | It is a kind of to prepare the air flow bed pyrolysis oven vented one's spleen rich in methane thermal and system | |
| CN104277855B (en) | Electric heating low-temperature dry distillation furnace, low-temperature dry distillation production device and semicoke production method | |
| CN102814149A (en) | Methanation furnace for producing methane from coal synthesis gas and production method of methanation furnace | |
| CN205710605U (en) | The reaction unit of synthesis gas is prepared for methane and carbon dioxide catalytic reforming | |
| CN104804752A (en) | Timber continuous carbonization and gasification method and device | |
| CN101734657B (en) | Method for continuously preparing active semicoke and dedicated device therefor | |
| CN108394902B (en) | Carbon disulfide production system and method |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20110105 Effective date of abandoning: 20121003 |
|
| AV01 | Patent right actively abandoned |
Granted publication date: 20110105 Effective date of abandoning: 20121003 |